TW201630071A - Substrate processing apparatus - Google Patents

Substrate processing apparatus Download PDF

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TW201630071A
TW201630071A TW104136770A TW104136770A TW201630071A TW 201630071 A TW201630071 A TW 201630071A TW 104136770 A TW104136770 A TW 104136770A TW 104136770 A TW104136770 A TW 104136770A TW 201630071 A TW201630071 A TW 201630071A
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Taiwan
Prior art keywords
substrate
reaction gas
region
axis
processing apparatus
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TW104136770A
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Chinese (zh)
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TWI627675B (en
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岩崎征英
反田雄太
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東京威力科創股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/50Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating using electric discharges
    • C23C16/511Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating using electric discharges using microwave discharges
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/4412Details relating to the exhausts, e.g. pumps, filters, scrubbers, particle traps
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • C23C16/45525Atomic layer deposition [ALD]
    • C23C16/45527Atomic layer deposition [ALD] characterized by the ALD cycle, e.g. different flows or temperatures during half-reactions, unusual pulsing sequence, use of precursor mixtures or auxiliary reactants or activations
    • C23C16/45536Use of plasma, radiation or electromagnetic fields
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • C23C16/45525Atomic layer deposition [ALD]
    • C23C16/45544Atomic layer deposition [ALD] characterized by the apparatus
    • C23C16/45548Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32Gas-filled discharge tubes
    • H01J37/32009Arrangements for generation of plasma specially adapted for examination or treatment of objects, e.g. plasma sources
    • H01J37/32192Microwave generated discharge
    • H01J37/32211Means for coupling power to the plasma
    • H01J37/3222Antennas
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32Gas-filled discharge tubes
    • H01J37/32431Constructional details of the reactor
    • H01J37/3244Gas supply means
    • H01J37/32449Gas control, e.g. control of the gas flow

Abstract

A substrate processing apparatus includes: a mounting table configured to place a substrate thereon to be rotatable around an axis; an antenna provided in a first region; and a reaction gas supply section configured to supply a reaction gas to the first region. The reaction gas supply section includes an inside injection port and an outside injection port. The inside injection port is provided at a position closer to the axis than an antenna region when viewed in the axis direction, and configured to inject the reaction gas in a direction getting away from the axis. The outside injection port is provided at a position farther from the axis than the antenna region when viewed in the axis direction, and configured to inject the reaction gas in a direction approaching the axis at a flow rate controlled independently of that of the reaction gas injected from the inside injection port.

Description

基板處理裝置Substrate processing device

本案的各種樣態及實施形態係關於基板處理裝置。Various aspects and embodiments of the present invention relate to a substrate processing apparatus.

就在基板上施行成膜的方法而言,吾人已知電漿輔助原子層沉積(PE-ALD:Plasma Enhanced Atomic Layer Deposition)法。PE-ALD法係藉由將基板曝於前驅物氣體,而使含有薄膜的構成元素之前驅物氣體化學吸附在基板上。其次,將基板曝於沖洗氣體,藉以除去過量化學吸附在該基板的前驅物氣體。而且,藉由將基板曝於含有薄膜的構成元素之反應氣體的電漿,而在基板上形成期望的薄膜。PE-ALD法重複如此步驟,藉以在基板上產生膜,此膜含有前驅物氣體所含的原子或分子。As for the method of performing film formation on a substrate, a plasma enhanced Atomic Layer Deposition (PE-ALD) method is known. The PE-ALD method chemically adsorbs a precursor gas containing a constituent element of a thin film on a substrate by exposing the substrate to a precursor gas. Next, the substrate is exposed to a flushing gas to remove excess precursor gas that is chemically adsorbed on the substrate. Further, a desired film is formed on the substrate by exposing the substrate to a plasma containing a reaction gas of constituent elements of the film. The PE-ALD method repeats the step of producing a film on the substrate containing atoms or molecules contained in the precursor gas.

就實現PE-ALD法的一種裝置而言,吾人已知半批式成膜裝置。半批式成膜裝置之中,供給前驅物氣體的區域與產生反應氣體的電漿的區域係設在處理室內的個別的區域,且利用基板依序通過此等區域,而將期望厚度的膜產生在基板上。As far as a device for realizing the PE-ALD method is concerned, a semi-batch film forming device is known. In the semi-batch type film forming apparatus, a region in which a precursor gas is supplied and a region in which a plasma generating a reaction gas are generated are provided in individual regions in the processing chamber, and the substrate is sequentially passed through the regions to form a film having a desired thickness. Produced on the substrate.

如此成膜裝置包括載置台、噴淋頭、及電漿產生部。載置台支持基板,且以旋轉軸為中心旋轉。噴淋頭及電漿產生部係與載置台相向配置,且排列在周向。噴淋頭具有約略扇形的平面形狀,且將前驅物氣體供給至通過下方的被處理基板。電漿產生部自導波管將微波供給至約略扇形的天線,且自天線區域供給反應氣體,藉以在天線區域內產生反應氣體的電漿。噴淋頭的周圍及電漿產生部的周圍設有排氣口,且噴淋頭的周緣設有供給沖洗氣體的噴射口。 [先前技術文獻] [專利文獻] 請參照國際公開第2013/122043號。 [發明概要]The film forming apparatus thus includes a mounting table, a shower head, and a plasma generating portion. The stage supports the substrate and rotates around the rotation axis. The shower head and the plasma generating unit are disposed opposite to the mounting table and arranged in the circumferential direction. The shower head has a substantially fan-shaped planar shape and supplies precursor gas to the substrate to be processed passing under. The plasma generating portion supplies the microwave to the approximately sector-shaped antenna from the waveguide, and supplies the reaction gas from the antenna region, thereby generating a plasma of the reaction gas in the antenna region. An exhaust port is provided around the shower head and around the plasma generating portion, and an injection port for supplying the flushing gas is provided on the periphery of the shower head. [Prior Art Document] [Patent Document] Please refer to International Publication No. 2013/122043. [Summary of the Invention]

本發明所揭示之基板處理裝置包括:載置台,載置被處理基板,且設置成能以前述軸線為中心旋轉,以使前述被處理基板在軸線周圍移動;天線,設在電漿處理區域,其係由載置台的旋轉而對著前述軸線繞周向移動之前述被處理基板所依序通過的多個區域之中的一個區域;以及氣體供給部,將反應氣體供給至前述電漿處理區域;且前述氣體供給部具有:內側噴射口,從前述軸線方向觀察之情形下,係設在前述天線與前述軸線之間,且從比前述天線更靠近前述軸線的位置,往遠離前述軸線之方向噴射反應氣體;以及外側噴射口,從前述軸線方向觀察之情形下,係設在比前述天線更遠離前述軸線的位置,且從比前述天線更遠離前述軸線的位置,往接近前述軸線的方向噴射反應氣體,此反應氣體的流量與從前述內側噴射口噴射之反應氣體的流量係受到獨立控制。A substrate processing apparatus according to the present invention includes: a mounting table on which a substrate to be processed is placed, and is rotatable about the axis to move the substrate to be processed around the axis; and the antenna is disposed in the plasma processing region. One of a plurality of regions sequentially passing through the substrate to be processed which is circumferentially moved toward the axis by the rotation of the mounting table; and a gas supply portion that supplies the reaction gas to the plasma processing region And the gas supply unit has an inner injection port that is disposed between the antenna and the axis when viewed in the axial direction, and is away from the axis from a position closer to the axis than the antenna. The injection reaction gas; and the outer injection port are disposed at a position farther from the axis than the antenna when viewed from the axial direction, and are ejected in a direction close to the axis from a position farther from the axis than the antenna. a reaction gas, the flow rate of the reaction gas and the flow rate of the reaction gas injected from the inner injection port are unique Control.

上述概要僅用以說明,不意圖以任何方式進行限制。上述說明性樣態、實施例、特徵,以及追加性樣態、實施例、特徵,由參照圖面和以下詳細說明而更明確。The above summary is for illustrative purposes only and is not intended to be limiting in any way. The above-described illustrative aspects, embodiments, features, and additional aspects, embodiments, and features are more apparent from the detailed description of the drawings.

以下詳細說明係參照形成一部分說明書之附加圖式。詳細說明、圖面、及請求項所記載之說明性實施例非意圖限制。可以不超脫於此所示之本案的精神或範圍而使用其它實施例、或施行其它變形。The following detailed description refers to additional figures that form part of the specification. The illustrative embodiments described in the detailed description, drawings, and claims are not intended to be limiting. Other embodiments may be utilized, or other variants may be practiced without departing from the spirit or scope of the invention.

[發明所欲解決之問題] 上述文獻所記載之半批式成膜裝置之中,從載置台的旋轉中心至載置台的徑向之基板上的膜厚分布相較於載置台的旋轉方向之膜厚分布,均勻性更低。因此,吾人希望提昇半批式成膜裝置之中從載置台的旋轉中心至載置台的徑向之基板上的膜厚均勻性等膜厚分布的控制性。 [解決問題之方式][Problems to be Solved by the Invention] In the semi-batch type film forming apparatus described in the above document, the film thickness distribution on the substrate from the rotation center of the mounting table to the radial direction of the mounting table is smaller than the rotation direction of the mounting table. The film thickness is distributed and the uniformity is lower. Therefore, it is desired to improve the controllability of the film thickness distribution such as the film thickness uniformity on the substrate from the rotation center of the mounting table to the radial direction of the mounting table in the half batch type film forming apparatus. [The way to solve the problem]

本發明所揭示之基板處理裝置的一實施形態包括載置台、天線、氣體供給部。載置台載置被處理基板,且設置成能以軸線為中心旋轉,以使被處理基板軸線的周圍在移動。天線設在電漿處理區域,其係由載置台的旋轉而對著軸線繞周向移動之被處理基板所依序通過的多個區域之中的一個區域。氣體供給部將反應氣體供給至電漿處理區域。氣體供給部具有內側噴射口、外側噴射口。從軸線方向觀察之情形下,內側噴射口係設在天線與軸線之間,且從比天線更靠近軸線的位置,往遠離軸線的方向噴射反應氣體。從軸線方向觀察之情形下,外側噴射口係設在比天線更遠離軸線的位置,且從比天線更遠離軸線的位置往接近軸線之方向噴射反應氣體,此反應氣體的流量與從內側噴射口噴射之反應氣體的流量係受到獨立控制。An embodiment of the substrate processing apparatus disclosed in the present invention includes a mounting table, an antenna, and a gas supply unit. The stage is placed on the substrate to be processed, and is set to be rotatable about the axis so that the periphery of the axis of the substrate to be processed is moved. The antenna is provided in a plasma processing region, which is one of a plurality of regions sequentially passing through the substrate to be processed which is moved circumferentially about the axis by the rotation of the mounting table. The gas supply unit supplies the reaction gas to the plasma processing region. The gas supply unit has an inner injection port and an outer injection port. In the case of viewing from the axial direction, the inner injection port is provided between the antenna and the axis, and the reaction gas is ejected in a direction away from the axis from a position closer to the axis than the antenna. When viewed from the axial direction, the outer injection port is disposed at a position farther from the axis than the antenna, and the reaction gas is ejected from a position farther from the axis than the antenna toward the axis, and the flow rate of the reaction gas is from the inner injection port. The flow rate of the injected reaction gas is independently controlled.

此外,本發明揭示之基板處理裝置的一實施形態之中,從軸線方向觀察之情形下,內側噴射口及外側噴射口將反應氣體噴設至設有天線的區域。Further, in an embodiment of the substrate processing apparatus according to the present invention, when viewed from the axial direction, the inner injection port and the outer injection port discharge the reaction gas to a region where the antenna is provided.

此外,本發明揭示之一實施形態之中,內側噴射口及外側噴射口將反應氣體噴射至與載置台所載置之被處理基板的面平行的方向。Further, in an embodiment of the present invention, the inside injection port and the outside injection port spray the reaction gas in a direction parallel to the surface of the substrate to be processed placed on the mounting table.

此外,本發明揭示之基板處理裝置的一實施形態之中,氣體供給部具有多個內側噴射口及外側噴射口。Further, in an embodiment of the substrate processing apparatus according to the present invention, the gas supply unit has a plurality of inner injection ports and outer injection ports.

此外,本發明揭示之一實施形態之中,天線係在電漿處理區域設置多個。內側噴射口及外側噴射口係在每一天線分別分配一個以上,且每一天線噴射之反應氣體的流量能受到獨立控制。Further, in an embodiment of the present invention, the antenna is provided in plurality in the plasma processing region. The inner injection port and the outer injection port are respectively assigned one or more at each antenna, and the flow rate of the reaction gas injected by each antenna can be independently controlled.

此外,本發明揭示之一實施形態之中,基板處理裝置更包括:排氣區域,沿著載置台的周緣而設,且由多個排氣孔進行排氣。從軸線方向觀察之情形下,排氣部係設在與設有天線之角度區域不同的區域。Further, in one embodiment of the present invention, the substrate processing apparatus further includes an exhaust region that is provided along a circumference of the mounting table and that is exhausted by the plurality of exhaust holes. When viewed from the axial direction, the exhaust portion is provided in a region different from the angular region in which the antenna is provided.

此外,本發明揭示之一實施形態之中,排氣區域係沿著載置台的周緣而設置多個。Further, in an embodiment of the present invention, the exhaust region is provided along the periphery of the mounting table.

此外,本發明揭示之一實施形態之中,來自各個排氣區域之排氣量係相同。 〔發明之效果〕Further, in one embodiment of the present invention, the amount of exhaust gas from each of the exhaust regions is the same. [Effects of the Invention]

依據本案揭示之基板處理裝置的一態樣,能提昇從載置台的旋轉中心至載置台的徑向之基板上膜厚分布的控制性。According to an aspect of the substrate processing apparatus disclosed in the present invention, it is possible to improve the controllability of the film thickness distribution on the substrate from the rotation center of the mounting table to the radial direction of the mounting table.

以下基於圖式詳細說明本案揭示之基板處理裝置的實施形態。另外,本案揭示之發明不因為本實施形態而受到限定。各實施形態可於不使處理內容矛盾的範圍下適當組合。Hereinafter, embodiments of the substrate processing apparatus disclosed in the present invention will be described in detail based on the drawings. Further, the invention disclosed in the present invention is not limited by the embodiment. Each embodiment can be appropriately combined without departing from the scope of the processing.

[實施發明之較佳形態] 圖1係顯示基板處理裝置10的一範例之剖面圖。圖2係顯示從上方觀察情形下之基板處理裝置10的一範例之模式圖。圖2中的A-A剖面係圖1。圖3及圖4係顯示圖1中的軸線X之左側部分的一範例之放大剖面圖。圖5顯示單元U的底面之一範例。圖6係圖1中的軸線X之右側部分的一範例之放大剖面圖。圖1~圖6所示之基板處理裝置10主要包括處理容器12、載置台14、第一氣體供給部16、排氣部18、第二氣體供給部20、電漿產生部22。BEST MODE FOR CARRYING OUT THE INVENTION FIG. 1 is a cross-sectional view showing an example of a substrate processing apparatus 10. Fig. 2 is a schematic view showing an example of the substrate processing apparatus 10 in the case of viewing from above. The A-A cross section in Fig. 2 is shown in Fig. 1. 3 and 4 are enlarged cross-sectional views showing an example of the left side portion of the axis X in Fig. 1. Figure 5 shows an example of the bottom surface of unit U. Figure 6 is an enlarged cross-sectional view showing an example of the right side portion of the axis X in Figure 1. The substrate processing apparatus 10 shown in FIGS. 1 to 6 mainly includes a processing container 12, a mounting table 14, a first gas supply unit 16, an exhaust unit 18, a second gas supply unit 20, and a plasma generating unit 22.

如圖1所示,處理容器12具有下部構件12a及上部構件12b。下部構件12a具上方開口之略筒狀,且形成凹部,此凹部含有形成出處理室C的側壁及底壁。上部構件12b係具略筒狀的蓋體,且將下部構件12a的凹部的上部開口加以關蓋,藉以形成處理室C。下部構件12a與上部構件12b之間的外周部設有用以密閉處理室C之彈性密封構件,例如設有O型環。As shown in Fig. 1, the processing container 12 has a lower member 12a and an upper member 12b. The lower member 12a has a slightly cylindrical shape with an upper opening, and is formed with a concave portion including a side wall and a bottom wall forming the processing chamber C. The upper member 12b is provided with a substantially cylindrical lid body, and the upper opening of the concave portion of the lower member 12a is closed to form the processing chamber C. An outer peripheral portion between the lower member 12a and the upper member 12b is provided with an elastic sealing member for sealing the processing chamber C, for example, an O-ring is provided.

基板處理裝置10在由處理容器12形成之處理室C的內部具有載置台14。載置台14藉由驅動機構24而以軸線X為中心旋轉驅動。驅動機構24具有馬達等驅動裝置24a及旋轉軸24b,且安裝在處理容器12的下部構件12a。The substrate processing apparatus 10 has a mounting table 14 inside the processing chamber C formed by the processing container 12. The mounting table 14 is rotationally driven about the axis X by the drive mechanism 24. The drive mechanism 24 has a drive unit 24a such as a motor and a rotary shaft 24b, and is attached to the lower member 12a of the processing container 12.

旋轉軸24b以軸線X為中心軸線,延伸至處理室C的內部。旋轉軸24b藉由自驅動裝置24a傳達的驅動力而以軸線X為中心旋轉。載置台14係由旋轉軸24b支持中央部分。藉此,載置台14以軸線X為中心,隨著旋轉軸24b的旋轉而旋轉。另外,處理容器12的下部構件12a與驅動機構24之間設有將處理室C加以密閉之例如O型環等彈性密封構件。The rotating shaft 24b extends to the inside of the processing chamber C with the axis X as a central axis. The rotating shaft 24b is rotated about the axis X by the driving force transmitted from the driving device 24a. The mounting table 14 supports the central portion by the rotating shaft 24b. Thereby, the mounting table 14 rotates with the rotation of the rotating shaft 24b centering on the axis X. Further, between the lower member 12a of the processing container 12 and the drive mechanism 24, an elastic sealing member such as an O-ring that seals the processing chamber C is provided.

基板處理裝置10在處理室C內部的載置台14的下方具有:加熱器26,用以加熱載置台14所載置之被處理基板即基板W。具體而言,加熱器26藉由加熱載置台14而加熱基板W。The substrate processing apparatus 10 has a heater 26 under the mounting table 14 inside the processing chamber C for heating the substrate W which is the substrate to be processed placed on the mounting table 14. Specifically, the heater 26 heats the substrate W by heating the mounting table 14.

處理容器12如圖2所示,係以軸線X為中心軸之略圓筒狀的容器,且在內部具備處理室C。在處理室C將具備噴射部16a的單元U加以設置。處理容器12例如係利用內面施行有防蝕鋁處理或Y2O3(氧化釔)之熔射處理等耐電漿處理之Al(鋁)等金屬而形成。基板處理裝置10在處理容器12內具有多個電漿產生部22。As shown in FIG. 2, the processing container 12 is a substantially cylindrical container having the axis X as a central axis, and has a processing chamber C therein. The unit U provided with the injection portion 16a is provided in the processing chamber C. The processing container 12 is formed, for example, by using a metal such as Al (aluminum) which is subjected to plasma treatment such as alumite treatment or Y2O3 (yttria) spraying treatment on the inner surface. The substrate processing apparatus 10 has a plurality of plasma generating portions 22 in the processing container 12.

各個電漿產生部22在處理容器12的上部具備將微波加以輸出的天線22a。本實施形態之中,各個天線22a的外形係帶有圓角的三角形。此外,從軸線X的方向觀察之情形下,各個天線22a的外形存在三條直線狀的邊,該三條邊係含於圍繞天線22a外形的三角形的邊。本實施形態之中,從軸線X的方向觀察之情形下,圍繞天線22a外形的三角形例如係正三角形,且相鄰的邊所成之角度例如係60°。圖2之中,處理容器12的上部設有三個天線22a,但天線22a的數量不限定於此,二個以下亦可,且即使四個以上亦可。Each of the plasma generating units 22 includes an antenna 22a that outputs microwaves at an upper portion of the processing container 12. In the present embodiment, the outer shape of each antenna 22a is a triangle having rounded corners. Further, in the case of viewing from the direction of the axis X, the outer shape of each antenna 22a has three straight sides which are included in the sides of the triangle surrounding the outer shape of the antenna 22a. In the present embodiment, when viewed from the direction of the axis X, the triangle surrounding the outer shape of the antenna 22a is, for example, an equilateral triangle, and the angle formed by the adjacent sides is, for example, 60°. In FIG. 2, three antennas 22a are provided in the upper portion of the processing container 12. However, the number of the antennas 22a is not limited thereto, and two or less may be used, and even four or more may be used.

基板處理裝置10例如圖2所示,包括:載置台14,在頂面具有多個基板載置區域14a。載置台14係以軸線X為中心軸之略圓板狀的構件。在載置台14的頂面,將載置基板W的多個(圖2之例中係五個)基板載置區域14a以軸線X為中心形成為同心圓狀。基板W配置在基板載置區域14a內,且載置台14旋轉之際,基板載置區域14a以基板W不偏移的方式支持基板W。基板載置區域14a與略圓狀的基板W係約略同形狀之略圓狀的凹部。基板載置區域14a的凹部的直徑相較於基板載置區域14a所載置之基板W的直徑W1,係約略相同。亦即,基板載置區域14a的凹部的直徑只要係以下述方式將基板W加以固定的程度即可:所載置之基板W嵌合於凹部,且即使載置台14旋轉,基板W亦不因離心力而自嵌合位置移動。As shown in FIG. 2, for example, the substrate processing apparatus 10 includes a mounting table 14 having a plurality of substrate mounting regions 14a on the top surface. The mounting table 14 is a substantially disk-shaped member having the axis X as a central axis. On the top surface of the mounting table 14, a plurality of (five in the example of FIG. 2) substrate mounting regions 14a on which the substrate W is placed are formed concentrically around the axis X. When the substrate W is placed in the substrate mounting region 14a and the mounting table 14 is rotated, the substrate mounting region 14a supports the substrate W so that the substrate W does not shift. The substrate mounting region 14a and the substantially circular substrate W are approximately circular recesses having substantially the same shape. The diameter of the concave portion of the substrate mounting region 14a is approximately the same as the diameter W1 of the substrate W placed on the substrate mounting region 14a. In other words, the diameter of the concave portion of the substrate mounting region 14a is such that the substrate W is fixed to the extent that the substrate W is placed in the concave portion, and the substrate W is not caused by the rotation of the mounting table 14 The centrifugal force moves from the fitting position.

基板處理裝置10在處理容器12的外緣,包括經由機械臂等搬運裝置而將基板W搬入處理室C、且將基板W從處理室C搬出之閘閥G。此外,基板處理裝置10在載置台14的外緣的下方,沿著載置台14的周緣而包括排氣部22h。排氣部22h連接排氣裝置52。從軸線X的方向觀察之情形下,排氣部22h於載置台14的旋轉方向之中,在設有天線22a之角度θ1的區域所鄰接之角度θ2的區域具有多個排氣孔。基板處理裝置10控制排氣裝置52的運作,並由排氣孔將處理室C內的氣體加以排氣,藉以將處理室C內的壓力維持在目標壓力。The substrate processing apparatus 10 includes a gate valve G that carries the substrate W into the processing chamber C and carries the substrate W out of the processing chamber C via a conveying device such as a robot arm at the outer edge of the processing container 12 . Further, the substrate processing apparatus 10 includes an exhaust portion 22h along the periphery of the mounting table 14 below the outer edge of the mounting table 14. The exhaust unit 22h is connected to the exhaust unit 52. When viewed from the direction of the axis X, the exhaust portion 22h has a plurality of exhaust holes in a region of the angle θ2 adjacent to the region where the angle θ1 of the antenna 22a is provided in the rotational direction of the mounting table 14. The substrate processing apparatus 10 controls the operation of the exhaust apparatus 52, and exhausts the gas in the processing chamber C by the exhaust holes, thereby maintaining the pressure in the processing chamber C at the target pressure.

處理室C例如圖2所示,包含排列在以軸線X為中心的圓周上之第一區域R1及第二區域R2。基板載置區域14a所載置之基板W,伴隨載置台14的旋轉而依序通過第一區域R1及第二區域R2。本實施形態之中,從上觀察之情形下,圖2所示之載置台14例如往順時針方向旋轉。第二區域R2係電漿處理區域的一範例。The processing chamber C includes, for example, as shown in FIG. 2, a first region R1 and a second region R2 arranged on a circumference centered on the axis X. The substrate W placed on the substrate mounting region 14a sequentially passes through the first region R1 and the second region R2 in accordance with the rotation of the mounting table 14. In the present embodiment, when viewed from above, the mounting table 14 shown in Fig. 2 is rotated in the clockwise direction, for example. The second region R2 is an example of a plasma processing region.

第一氣體供給部16例如圖3及圖4所示,具有內側氣體供給部161、中間氣體供給部162、及外側氣體供給部163。此外,第一區域R1的上方例如圖3及圖4所示,以相向於載置台14之頂面的方式設置:單元U,施行氣體之供給、沖洗、及排氣。單元U具按順序堆疊有第一構件M1、第二構件M2、第三構件M3、及第四構件M4之構造。單元U以抵接於處理容器12的上部構件12b的底面之方式安裝在處理容器12。The first gas supply unit 16 includes an inner gas supply unit 161, an intermediate gas supply unit 162, and an outer air supply unit 163, as shown in FIGS. 3 and 4, for example. Further, as shown in FIGS. 3 and 4, for example, as shown in FIG. 3 and FIG. 4, the first region R1 is provided with a unit U for supplying, flushing, and exhausting gas. The unit U has a configuration in which the first member M1, the second member M2, the third member M3, and the fourth member M4 are stacked in this order. The unit U is attached to the processing container 12 in such a manner as to abut against the bottom surface of the upper member 12b of the processing container 12.

單元U例如圖3及圖4所示,形成有貫穿第二構件M2~第四構件M4之氣體供給道161p、氣體供給道162p、及氣體供給道163p。氣體供給道161p連接至上端係設在處理容器12的上部構件12b之氣體供給道121p。氣體供給道121p經由閥161v及質流控制器等流量控制器161c,而連接前驅物氣體的氣體供給源16g。此外,氣體供給道161p的下端係連接於緩衝空間161d,此緩衝空間161d形成在第一構件M1與第二構件M2之間,且例如受到O型環等彈性構件161b圍繞。緩衝空間161d連接第一構件M1所設之內側噴射部161a的噴射口16h。For example, as shown in FIGS. 3 and 4, the unit U has a gas supply passage 161p, a gas supply passage 162p, and a gas supply passage 163p that penetrate the second member M2 to the fourth member M4. The gas supply path 161p is connected to the gas supply path 121p whose upper end is provided in the upper member 12b of the processing container 12. The gas supply path 121p is connected to the gas supply source 16g of the precursor gas via the flow rate controller 161c such as the valve 161v and the mass flow controller. Further, the lower end of the gas supply path 161p is connected to the buffer space 161d which is formed between the first member M1 and the second member M2, and is surrounded by, for example, an elastic member 161b such as an O-ring. The buffer space 161d is connected to the injection port 16h of the inner injection portion 161a provided in the first member M1.

此外,氣體供給道162p連接至上端係設在處理容器12的上部構件12b之氣體供給道122p。氣體供給道122p經由閥162v及質流控制器等流量控制器162c而連接前驅物氣體的氣體供給源16g。此外,氣體供給道162p的下端連接於緩衝空間162d,此緩衝空間162d形成在第一構件M1與第二構件M2之間、且例如受到O型環等彈性構件162b圍繞。緩衝空間162d連接第一構件M1所設之中間噴射部162a的噴射口16h。Further, the gas supply path 162p is connected to the gas supply path 122p whose upper end is provided in the upper member 12b of the processing container 12. The gas supply path 122p is connected to the gas supply source 16g of the precursor gas via the flow rate controller 162c such as the valve 162v and the mass flow controller. Further, the lower end of the gas supply path 162p is connected to the buffer space 162d which is formed between the first member M1 and the second member M2 and is surrounded by, for example, an elastic member 162b such as an O-ring. The buffer space 162d is connected to the ejection opening 16h of the intermediate ejection portion 162a provided in the first member M1.

此外,氣體供給道163p連接至上端設在處理容器12的上部構件12b之氣體供給道123p。氣體供給道123p經由閥163v及質流控制器等流量控制器163c而連接前驅物氣體的氣體供給源16g。此外,氣體供給道163p的下端連接於緩衝空間163d,此緩衝空間163d形成在第一構件M1與第二構件M2之間、且例如受到O型環等彈性構件163b圍繞。緩衝空間163d連接第一構件M1所設之外側噴射部163a的噴射口16h。Further, the gas supply path 163p is connected to the gas supply path 123p whose upper end is provided in the upper member 12b of the processing container 12. The gas supply path 123p is connected to the gas supply source 16g of the precursor gas via the flow rate controller 163c such as the valve 163v and the mass flow controller. Further, the lower end of the gas supply path 163p is connected to the buffer space 163d which is formed between the first member M1 and the second member M2 and is surrounded by, for example, an elastic member 163b such as an O-ring. The buffer space 163d is connected to the ejection port 16h of the outer side ejection portion 163a provided in the first member M1.

內側氣體供給部161的緩衝空間161d、中間氣體供給部162的緩衝空間162d、及外側氣體供給部163的緩衝空間163d例如圖3及圖4所示,形成獨立的空間。而且,通行在各個緩衝空間之前驅物氣體的流量係由流量控制器161c、流量控制器162c、及流量控制器163c而分別受到獨立控制。The buffer space 161d of the inside air supply unit 161, the buffer space 162d of the intermediate gas supply unit 162, and the buffer space 163d of the outside air supply unit 163 form an independent space as shown in, for example, FIGS. 3 and 4 . Further, the flow rate of the driving gas before the respective buffer spaces is independently controlled by the flow controller 161c, the flow controller 162c, and the flow controller 163c.

單元U例如圖3及圖4所示,形成貫穿第四構件M4之氣體供給道20r。氣體供給道20r連接至上端係設在處理容器12的上部構件12b之氣體供給道12r。氣體供給道12r經由閥20v及流量控制器20c而連接有沖洗氣體的氣體供給源20g。The unit U forms a gas supply path 20r penetrating the fourth member M4 as shown in Figs. 3 and 4, for example. The gas supply path 20r is connected to the gas supply path 12r whose upper end is provided in the upper member 12b of the processing container 12. The gas supply path 12r is connected to the gas supply source 20g of the flushing gas via the valve 20v and the flow rate controller 20c.

氣體供給道20r的下端連接至設在第四構件M4的底面與第三構件M3的頂面之間的空間20d。此外,第四構件M4形成將第一構件M1~第三構件M3加以收容的凹部。在形成凹部之第四構件M4的內側面與第三構件M3的外側面之間設置間隙20p。間隙20p連接於空間20d。間隙20p的下端係作為噴射口20a而發揮功能。The lower end of the gas supply path 20r is connected to a space 20d provided between the bottom surface of the fourth member M4 and the top surface of the third member M3. Further, the fourth member M4 forms a recess in which the first member M1 to the third member M3 are housed. A gap 20p is provided between the inner side surface of the fourth member M4 forming the recess and the outer side surface of the third member M3. The gap 20p is connected to the space 20d. The lower end of the gap 20p functions as the injection port 20a.

在單元U例如圖3及圖4所示,將貫穿第三構件M3及第四構件M4的排氣道18q加以形成。排氣道18q連接至上端係設在處理容器12的上部構件12b之排氣道12q。排氣道12q連接至真空泵等排氣裝置34。此外,排氣道18q連接至下端係設在第三構件M3的底面與第二構件M2的頂面之間之空間18d。In the unit U, for example, as shown in FIGS. 3 and 4, the exhaust passage 18q penetrating the third member M3 and the fourth member M4 is formed. The exhaust passage 18q is connected to the exhaust passage 12q whose upper end is attached to the upper member 12b of the processing container 12. The exhaust passage 12q is connected to an exhaust device 34 such as a vacuum pump. Further, the exhaust passage 18q is connected to a space 18d which is provided at a lower end between the bottom surface of the third member M3 and the top surface of the second member M2.

第三構件M3包括將第一構件M1及第二構件M2加以收容的凹部。在第三構件M3的內側面與第一構件M1及第二構件M2的外側面之間,設置間隙18g,此第三構件M3的內側面構成第三構件M3所具備的凹部。空間18d連接於間隙18g。間隙18g的下端係作為排氣口18a而發揮功能。The third member M3 includes a recess in which the first member M1 and the second member M2 are housed. A gap 18g is provided between the inner side surface of the third member M3 and the outer surface of the first member M1 and the second member M2, and the inner side surface of the third member M3 constitutes a recess provided in the third member M3. The space 18d is connected to the gap 18g. The lower end of the gap 18g functions as the exhaust port 18a.

在單元U的底面即與載置台14相向的面,例如圖5所示,沿著脫離軸線X的方向即Y軸方向而設置噴射部16a。處理室C所含之區域中的噴射部16a所相向之區域係第一區域R1。噴射部16a將前驅物氣體噴射至載置台14上的基板W。噴射部16a例如圖5所示,具有內側噴射部161a、中間噴射部162a、及外側噴射部163a。The bottom surface of the unit U, that is, the surface facing the mounting table 14, for example, as shown in FIG. 5, the ejection portion 16a is provided along the direction of the disengagement axis X, that is, the Y-axis direction. The region in which the ejection portion 16a in the region included in the processing chamber C faces is the first region R1. The injection portion 16a injects the precursor gas onto the substrate W on the mounting table 14. For example, as shown in FIG. 5, the injection portion 16a has an inner injection portion 161a, an intermediate injection portion 162a, and an outer injection portion 163a.

內側噴射部161a例如圖5所示,形成在自軸線X起算的距離係位於r1~r2之範圍的環狀區域中之含於單元U的底面之區域即內側環狀區域A1內。此外,中間噴射部162a形成在自軸線X起算的距離係位於r2~r3之範圍的環狀區域中之含於單元U的底面之區域即中間環狀區域A2內。此外,外側噴射部163a形成在自軸線X起算的距離係位於r3~r4之範圍的環狀區域中之含於單元U的底面之區域即外側環狀區域A3內。For example, as shown in FIG. 5, the inner jetting portion 161a is formed in the inner annular region A1 which is a region included in the bottom surface of the unit U in the annular region in the range from r1 to r2, which is the distance from the axis X. Further, the intermediate injection portion 162a is formed in the intermediate annular region A2 which is a region included in the bottom surface of the unit U in the annular region in which the distance from the axis X is in the range of r2 to r3. Further, the outer injection portion 163a is formed in the outer annular region A3 which is a region included in the bottom surface of the unit U in the annular region in which the distance from the axis X is in the range of r3 to r4.

例如圖5所示,單元U的底面所形成之噴射部16a在Y軸方向延伸的範圍即自r1到r4為止的長度L相較於直徑W1的基板W通過Y軸的長度,在軸線X側之方向更長既定距離ΔL以上、在軸線X側之反方向更長既定距離ΔL以上。For example, as shown in FIG. 5, the length L of the injection portion 16a formed on the bottom surface of the unit U in the Y-axis direction, that is, the length L from r1 to r4 is longer than the length of the substrate W of the diameter W1 on the axis X side. The direction is longer than the predetermined distance ΔL, and the opposite direction on the axis X side is longer than the predetermined distance ΔL.

內側噴射部161a、中間噴射部162a、及外側噴射部163a例如圖5所示,包括多個噴射口16h。前驅物氣體從各個噴射口16h往第一區域R1噴射。從內側噴射部161a、中間噴射部162a、及外側噴射部163a各者的噴射口16h往第一區域R1噴射之前驅物氣體的流量,係由流量控制器161c、流量控制器162c、及流量控制器163c而分別受到獨立控制。將前驅物氣體供給至第一區域R1,藉以使前驅物氣體的原子或分子化學性吸附在已通過第一區域R1之基板W的表面。前驅物氣體例如係DCS(二氯矽烷)、一氯甲硅烷、三氯矽烷、六氯矽烷等。The inner injection portion 161a, the intermediate injection portion 162a, and the outer injection portion 163a include a plurality of injection ports 16h as shown in FIG. 5, for example. The precursor gas is ejected from the respective ejection ports 16h to the first region R1. The flow rate of the precursor gas injected from the injection port 16h of each of the inner injection portion 161a, the intermediate injection portion 162a, and the outer injection portion 163a to the first region R1 is controlled by the flow rate controller 161c, the flow rate controller 162c, and the flow rate. The device 163c is independently controlled. The precursor gas is supplied to the first region R1, whereby the atoms or molecules of the precursor gas are chemically adsorbed on the surface of the substrate W that has passed through the first region R1. The precursor gas is, for example, DCS (dichlorodecane), monochlorosilane, trichlorodecane, hexachlorodecane or the like.

例如圖3及圖4所示,第一區域R1的上方以相向於載置台14的頂面之方式設有排氣部18的排氣口18a。排氣口18a例如圖5所示,以圍繞噴射部16a的周圍之方式形成在單元U的底面。排氣口18a藉由真空泵等排氣裝置34的運作,經由排氣口18a而將處理室C內的氣體加以排氣。For example, as shown in FIGS. 3 and 4, the upper portion of the first region R1 is provided with an exhaust port 18a of the exhaust portion 18 so as to face the top surface of the mounting table 14. The exhaust port 18a is formed on the bottom surface of the unit U so as to surround the periphery of the injection portion 16a as shown, for example, in FIG. The exhaust port 18a exhausts the gas in the processing chamber C through the exhaust port 18a by the operation of the exhaust device 34 such as a vacuum pump.

在第一區域R1的上方,例如圖3及圖4所示,以相向於載置台14的頂面之方式設有第二氣體供給部20的噴射口20a。噴射口20a例如圖5所示,以圍繞排氣口18a的周圍之方式形成在單元U的底面。第二氣體供給部20經由噴射口20a而往第一區域R1噴射沖洗氣體。第二氣體供給部20所噴射之沖洗氣體係例如Ar(氬)等惰性氣體。藉由將沖洗氣體噴射至基板W的表面,而從基板W去除過量吸附在基板W之前驅物氣體的原子或分子(残留氣體成分)。藉此,在基板W的表面將化學吸附有前驅物氣體的原子或分子之原子層或分子層加以形成。Above the first region R1, for example, as shown in Figs. 3 and 4, the injection port 20a of the second gas supply portion 20 is provided so as to face the top surface of the mounting table 14. The injection port 20a is formed on the bottom surface of the unit U so as to surround the periphery of the exhaust port 18a as shown, for example, in FIG. The second gas supply unit 20 injects the flushing gas into the first region R1 via the injection port 20a. The flushing gas system injected by the second gas supply unit 20 is, for example, an inert gas such as Ar (argon). By spraying the flushing gas onto the surface of the substrate W, atoms or molecules (residual gas components) of the precursor gas adsorbed excessively before the substrate W are removed from the substrate W. Thereby, an atomic layer or a molecular layer of an atom or a molecule to which a precursor gas is chemically adsorbed is formed on the surface of the substrate W.

單元U從噴射口20a噴射沖洗氣體,且沿著載置台14的表面而由排氣口18a將沖洗氣體加以排氣。藉此,單元U抑制供給至第一區域R1的前驅物氣體漏出至第一區域R1外。此外,因為單元U從噴射口20a噴射沖洗氣體且沿著載置台14的面而由排氣口18a將氣體加以排氣,所以抑制供給至第二區域R2之反應氣體或反應氣體的自由基等侵入第一區域R1內。亦即,單元U藉由來自第二氣體供給部20之沖洗氣體的噴射及來自排氣部18的排氣,而隔離第一區域R1與第二區域R2。The unit U injects the flushing gas from the injection port 20a, and exhausts the flushing gas by the exhaust port 18a along the surface of the mounting table 14. Thereby, the unit U suppresses leakage of the precursor gas supplied to the first region R1 to the outside of the first region R1. Further, since the unit U injects the flushing gas from the injection port 20a and exhausts the gas through the exhaust port 18a along the surface of the mounting table 14, the radicals of the reaction gas or the reaction gas supplied to the second region R2 are suppressed. Invades into the first area R1. That is, the unit U isolates the first region R1 and the second region R2 by the injection of the flushing gas from the second gas supply portion 20 and the exhaust gas from the exhaust portion 18.

基板處理裝置10例如圖6所示,在位於第二區域R2的上方之上部構件12b的開口AP包括:電漿產生部22,設置成相向於載置台14的頂面。電漿產生部22具有:天線22a;同軸導波管22b,將微波供給至天線22a;以及反應氣體供給部22c,將反應氣體供給至第二區域R2。本實施形態之中,上部構件12b例如形成三個開口AP,且基板處理裝置10例如包括三個天線22a。As shown in FIG. 6 , for example, as shown in FIG. 6 , the substrate processing device 10 includes an electrode generating portion 22 that is disposed on the top surface of the mounting table 14 in the opening AP located above the second region R2 . The plasma generating unit 22 includes an antenna 22a, a coaxial waveguide 22b that supplies microwaves to the antenna 22a, and a reaction gas supply unit 22c that supplies the reaction gas to the second region R2. In the present embodiment, the upper member 12b is formed with, for example, three openings AP, and the substrate processing apparatus 10 includes, for example, three antennas 22a.

電漿產生部22自天線22a及同軸導波管22b將微波供給至第二區域R2,且自反應氣體供給部22c將反應氣體供給至第二區域R2,藉以在第二區域R2產生反應氣體的電漿。而且,電漿產生部22對化學性吸附在基板W之原子層或分子層施行電漿處理。本實施形態使用含氮氣體作為反應氣體,且電漿產生部22使化學吸附在基板W之原子層或分子層氮化。就反應氣體而言,例如能使用N2(氮)或NH3(氨)等含氮氣體。The plasma generating unit 22 supplies microwaves to the second region R2 from the antenna 22a and the coaxial waveguide 22b, and supplies the reaction gas to the second region R2 from the reaction gas supply portion 22c, thereby generating a reaction gas in the second region R2. Plasma. Further, the plasma generating unit 22 performs a plasma treatment on the atomic layer or the molecular layer chemically adsorbed on the substrate W. In the present embodiment, a nitrogen-containing gas is used as the reaction gas, and the plasma generating portion 22 nitifies the atomic layer or the molecular layer of the substrate W by chemical adsorption. As the reaction gas, for example, a nitrogen-containing gas such as N 2 (nitrogen) or NH 3 (ammonia) can be used.

電漿產生部22例如圖6所示,將天線22a氣密配置,用以封閉開口AP。天線22a具有天板40、槽孔板42、及慢波板44。天板40係以介電質形成之帶有圓角的略正三角形構件,例如利用氧化鋁陶瓷等形成。天板40以使其底面從處理容器12的上部構件12b所形成之開口AP露出在第二區域R2的方式由上部構件12b支持。The plasma generating unit 22, for example, as shown in FIG. 6, hermetically arranges the antenna 22a to close the opening AP. The antenna 22a has a sky plate 40, a slot plate 42, and a slow wave plate 44. The sky plate 40 is a slightly equilateral triangular member having a rounded corner formed of a dielectric material, for example, formed of alumina ceramic or the like. The top plate 40 is supported by the upper member 12b such that the bottom surface thereof is exposed from the opening AP formed by the upper member 12b of the processing container 12 in the second region R2.

在天板40的頂面設置槽孔板42。槽孔板42係形成為略正三角形之板狀的金屬製構件。槽孔板42形成有多個槽孔對。各槽孔對含有相互正交之之二個槽孔洞。A slot plate 42 is provided on the top surface of the top plate 40. The slot plate 42 is formed of a metal member having a substantially right triangular plate shape. The slot plate 42 is formed with a plurality of slot pairs. Each slot pair contains two slot holes that are orthogonal to each other.

槽孔板42的頂面設有慢波板44。慢波板44係以介電質形成之略正三角形的構件,例如由氧化鋁陶瓷等形成。在慢波板44設置:略圓筒狀的開口,用以配置同軸導波管22b的外側導體62b。The top surface of the slot plate 42 is provided with a slow wave plate 44. The slow wave plate 44 is a member having a substantially equilateral triangle formed of a dielectric material, for example, an alumina ceramic or the like. The slow wave plate 44 is provided with a slightly cylindrical opening for arranging the outer conductor 62b of the coaxial waveguide 22b.

在慢波板44的頂面設置金屬製的冷卻板46。冷卻板46藉由流通在其內部形成的流道之冷媒,而隔著慢波板44冷卻天線22a。冷卻板46藉由未圖示的彈簧等而按壓慢波板44的頂面,且冷卻板46的底面係與慢波板44的頂面密合。A metal cooling plate 46 is provided on the top surface of the slow wave plate 44. The cooling plate 46 cools the antenna 22a via the slow wave plate 44 by circulating the refrigerant in the flow path formed therein. The cooling plate 46 presses the top surface of the slow wave plate 44 by a spring or the like (not shown), and the bottom surface of the cooling plate 46 is in close contact with the top surface of the slow wave plate 44.

同軸導波管22b包括內側導體62a及外側導體62b。內側導體62a自天線22a的上方貫穿慢波板44的開口及槽孔板42的開口。外側導體62b在內側導體62a的外周面與外側導體62b的內周面之間空出縫隙而設置成圍繞內側導體62a。外側導體62b的下端連接於冷卻板46的開口部。另外,天線22a亦可作為電極而發揮功能。或者,亦可將處理容器12內所設之電極作為天線22a使用。The coaxial waveguide 22b includes an inner conductor 62a and an outer conductor 62b. The inner conductor 62a penetrates the opening of the slow wave plate 44 and the opening of the slot plate 42 from above the antenna 22a. The outer conductor 62b is provided to surround the inner conductor 62a with a gap between the outer circumferential surface of the inner conductor 62a and the inner circumferential surface of the outer conductor 62b. The lower end of the outer conductor 62b is connected to the opening of the cooling plate 46. Further, the antenna 22a can also function as an electrode. Alternatively, an electrode provided in the processing container 12 may be used as the antenna 22a.

基板處理裝置10具有導波管60及微波產生器68。微波產生器68所產生之例如約2.45GHz的微波係經由導波管60而傳遞至同軸導波管22b,且傳遞在內側導體62a與外側導體62b之縫隙。而且,傳遞在慢波板44內的微波自槽孔板42的槽孔洞往天板40傳遞,且自天板40往第二區域R2幅射。The substrate processing apparatus 10 has a waveguide 60 and a microwave generator 68. The microwave generated by the microwave generator 68, for example, about 2.45 GHz, is transmitted to the coaxial waveguide 22b via the waveguide 60, and is transmitted to the gap between the inner conductor 62a and the outer conductor 62b. Moreover, the microwaves transmitted in the slow wave plate 44 are transmitted from the slot holes of the slot plate 42 to the sky plate 40, and are radiated from the sky plate 40 to the second region R2.

反應氣體從反應氣體供給部22c供給至第二區域R2。反應氣體供給部22c具有多個內側噴射口50b及多個外側噴射口51b。各個內側噴射口50b經由閥50v及質流控制器等流量控制部50c而連接至反應氣體的氣體供給源50g。The reaction gas is supplied from the reaction gas supply unit 22c to the second region R2. The reaction gas supply unit 22c has a plurality of inner injection ports 50b and a plurality of outer injection ports 51b. Each of the inner injection ports 50b is connected to the gas supply source 50g of the reaction gas via a valve 50v and a flow rate control unit 50c such as a mass flow controller.

各個內側噴射口50b例如圖2及圖6所示,設在處理容器12的上部構件12b的底面。再者,從軸線X的方向觀察之情形下,各個內側噴射口50b所設之位置例如圖2及圖6所示,係較天線22a區域更靠近軸線X的位置。本實施形態之中,從軸線X的方向觀察之情形下,天線22a區域係例如在第二區域R2之中配置有天線22a的天板40之區域。Each of the inner injection ports 50b is provided on the bottom surface of the upper member 12b of the processing container 12, as shown in Figs. 2 and 6, for example. Further, when viewed from the direction of the axis X, the position of each of the inner injection ports 50b is, for example, as shown in Figs. 2 and 6, which is closer to the axis X than the region of the antenna 22a. In the present embodiment, when viewed from the direction of the axis X, the region of the antenna 22a is, for example, a region in which the antenna 40a of the antenna 22a is disposed in the second region R2.

多個內側噴射口50b係依既定數量分配在各天線22a。而且,分配在各個天線22a之既定數量的內側噴射口50b例如圖2所示,從軸線X的方向觀察之情形下,在載置台14的旋轉方向之設有天線22a之角度θ1的區域沿著載置台14的旋轉方向而配置。本實施形態之中,例如圖2所示,在各個天線22a分配三個內側噴射口50b。而且,三個內側噴射口50b係於載置台14的旋轉方向之設有天線22a之角度θ1的區域即60°的角度範圍內,例如以20°的間隔而分散配置。The plurality of inner injection ports 50b are distributed to the respective antennas 22a in a predetermined number. Further, a predetermined number of inner injection ports 50b allocated to the respective antennas 22a are viewed from the direction of the axis X as viewed in the direction of the axis X, and the region of the angle θ1 at which the antenna 22a is provided in the rotation direction of the stage 14 is along The mounting table 14 is disposed in the rotation direction. In the present embodiment, for example, as shown in Fig. 2, three inner injection ports 50b are allocated to the respective antennas 22a. Further, the three inner injection ports 50b are arranged in an angular range of 60° which is a region where the angle θ1 of the antenna 22a is provided in the rotation direction of the mounting table 14, and is, for example, dispersed at intervals of 20°.

而且,各個內側噴射口50b係經由閥50v及流量控制部50c,將由氣體供給源50g供給之反應氣體朝往遠離軸線X的方向,噴設至天線22a的下方的第二區域R2。本實施形態之中,各個內側噴射口50b例如將反應氣體噴射至載置台14的平面方向。各個內側噴射口50b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行的方向。Further, each of the inner injection ports 50b is caused to flow the reaction gas supplied from the gas supply source 50g to the second region R2 below the antenna 22a in the direction away from the axis X via the valve 50v and the flow rate control unit 50c. In the present embodiment, each of the inner injection ports 50b ejects the reaction gas to the planar direction of the mounting table 14, for example. Each of the inner injection ports 50b ejects, for example, a reaction gas into a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14.

各個外側噴射口51b經由閥51v及質流控制器等流量控制部51c,而連接至反應氣體的氣體供給源50g。各個外側噴射口51b例如圖2及圖6所示,設在處理容器12的上部構件12b的底面。再者,例如圖2及圖6所示,從軸線X的方向觀察之情形下,設置各個外側噴射口51b之位置係較天線22a區域更遠離軸線X的位置。Each of the outer injection ports 51b is connected to the gas supply source 50g of the reaction gas via the flow rate control unit 51c such as the valve 51v and the mass flow controller. Each of the outer injection ports 51b is provided on the bottom surface of the upper member 12b of the processing container 12, as shown in Figs. 2 and 6, for example. Further, for example, as shown in FIGS. 2 and 6, when viewed from the direction of the axis X, the position of each of the outer injection ports 51b is set to be farther from the axis X than the region of the antenna 22a.

此外,多個外側噴射口51b係依既定數量分配在各天線22a。而且,分配在各個天線22a之既定數量的外側噴射口51b例如圖2所示,從軸線X的方向觀察之情形下,在載置台14的旋轉方向之設有天線22a之角度θ1的區域沿著載置台14的旋轉方向而配置。本實施形態之中,在各個天線22a分配37個外側噴射口51b。而且,37個外側噴射口51b在載置台14的旋轉方向之設有天線22a之角度θ1的區域即60°的角度範圍內,例如以約1.6°的間隔分散配置。Further, a plurality of outer injection ports 51b are distributed to the respective antennas 22a in a predetermined number. Further, a predetermined number of outer injection ports 51b allocated to the respective antennas 22a are, as shown in FIG. 2, as viewed in the direction of the axis X, along the region where the angle θ1 of the antenna 22a is provided in the rotational direction of the stage 14 along The mounting table 14 is disposed in the rotation direction. In the present embodiment, 37 outer injection ports 51b are allocated to the respective antennas 22a. Further, the 37 outer injection ports 51b are disposed in an angular range of 60° which is a region where the angle θ1 of the antenna 22a is provided in the rotation direction of the mounting table 14, for example, at an interval of about 1.6°.

而且,各個外側噴射口51b經由閥51v及流量控制部51c而將由氣體供給源50g供給之反應氣體,朝往接近軸線X的方向而噴射至天線22a的下方的第二區域R2。本實施形態之中,各個外側噴射口51b例如將反應氣體噴射至載置台14的平面方向。各個外側噴射口51b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行之方向。此外,內側噴射口50b及外側噴射口51b例如圖6所示,係作為與將處理容器12從上方關蓋的上部構件12b或天線22a有別的構件而安裝在上部構件12b的底面。藉此,能容易將內側噴射口50b及外側噴射口51b自上部構件12b或天線22a卸除,且內側噴射口50b及外側噴射口51b的維修變得容易。Further, each of the outer injection ports 51b injects the reaction gas supplied from the gas supply source 50g to the second region R2 below the antenna 22a in the direction toward the axis X via the valve 51v and the flow rate control portion 51c. In the present embodiment, each of the outer injection ports 51b ejects the reaction gas to the planar direction of the mounting table 14, for example. Each of the outer injection ports 51b ejects, for example, a reaction gas into a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14. Further, the inner injection port 50b and the outer injection port 51b are attached to the bottom surface of the upper member 12b as a separate member from the upper member 12b or the antenna 22a that closes the processing container 12 from above, as shown in Fig. 6, for example. Thereby, the inner injection port 50b and the outer injection port 51b can be easily removed from the upper member 12b or the antenna 22a, and the maintenance of the inner injection port 50b and the outer injection port 51b becomes easy.

此外,本實施形態之中,從內側噴射口50b及外側噴射口51b噴射之反應氣體的流量係藉由流量控制部50c及流量控制部51c而分別受到獨立控制。再者,流量控制部50c及流量控制部51c亦可設在每一天線22a,且從內側噴射口50b及外側噴射口51b噴射之反應氣體的流量亦可在每一天線22a受到獨立控制。Further, in the present embodiment, the flow rate of the reaction gas injected from the inner injection port 50b and the outer injection port 51b is independently controlled by the flow rate control unit 50c and the flow rate control unit 51c. Further, the flow rate control unit 50c and the flow rate control unit 51c may be provided in each of the antennas 22a, and the flow rate of the reaction gas injected from the inner injection port 50b and the outer injection port 51b may be independently controlled for each antenna 22a.

電漿產生部22藉由多個內側噴射口50b及多個外側噴射口51b而將反應氣體供給至第二區域R2,且藉由天線22a而將微波幅射至第二區域R2。藉此,電漿產生部22在第二區域R2之中產生反應氣體的電漿。The plasma generating unit 22 supplies the reaction gas to the second region R2 via the plurality of inner injection ports 50b and the plurality of outer injection ports 51b, and radiates the microwaves to the second region R2 via the antenna 22a. Thereby, the plasma generating unit 22 generates a plasma of the reaction gas in the second region R2.

例如圖2所示,在載置台14周緣設置排氣部22h。排氣部22h例如圖6所示,具有:上部開口之溝部222;以及蓋部221,設在溝部222的上部。溝部222連接於排氣裝置52。從軸線X的方向觀察之情形下,蓋部221例如在圖2所示之基板處理裝置10之中,於載置台14的旋轉方向,在設有天線22a之角度θ1的區域所鄰接之角度θ2的區域即排氣區域220h具有多個排氣孔。另外,設有天線22之角度θ1的區域之中,蓋部221未設有排氣孔。For example, as shown in FIG. 2, the exhaust portion 22h is provided on the periphery of the mounting table 14. For example, as shown in FIG. 6, the exhaust portion 22h has a groove portion 222 that is open at the upper portion, and a lid portion 221 that is provided at an upper portion of the groove portion 222. The groove portion 222 is connected to the exhaust device 52. When viewed from the direction of the axis X, the lid portion 221 is, for example, in the substrate processing apparatus 10 shown in FIG. 2, at an angle θ2 adjacent to the region where the angle θ1 of the antenna 22a is provided in the rotation direction of the mounting table 14. The area, that is, the exhaust area 220h has a plurality of exhaust holes. Further, among the regions where the angle θ1 of the antenna 22 is provided, the cover portion 221 is not provided with a vent hole.

此外,在係外側噴射口51b的下方且係蓋部221上,設置間隔件220。從軸線X的方向觀察之情形下,間隔件220設在係載置台14的周緣、且係於載置台14的旋轉方向之中設有天線22a之角度θ1的區域。間隔件220例如圖6所示,具有與從蓋部221的頂面至載置台14的頂面之高度約略相同的厚度。間隔件220在外側噴射口51b的下方,抑制因為載置台14與蓋部221的高低差而生之氣體流速的增加。Further, a spacer 220 is provided below the outer side ejection opening 51b and on the cap portion 221 . When viewed from the direction of the axis X, the spacer 220 is provided on the periphery of the mounting base 14 and is provided in a region where the angle θ1 of the antenna 22a is provided in the rotation direction of the mounting table 14. The spacer 220 has a thickness approximately the same as the height from the top surface of the lid portion 221 to the top surface of the mounting table 14, as shown in FIG. The spacer 220 is below the outer ejection opening 51b, and suppresses an increase in the gas flow rate due to the difference in height between the mounting table 14 and the lid portion 221.

排氣部22h在各個排氣區域220h,藉由排氣裝置52之運作,而由蓋部221所設之多個排氣孔經由溝部222而將處理室C內氣體加以排氣。另外,設在蓋部221的排氣孔調整各個排氣區域220h所設之排氣孔的位置、大小、數量,以使來自各個排氣區域220h的排氣量係約略相同。In each of the exhaust regions 220h, the exhaust portion 22h is operated by the exhaust device 52, and the plurality of exhaust holes provided in the lid portion 221 exhaust the gas in the processing chamber C via the groove portion 222. Further, the exhaust holes provided in the lid portion 221 adjust the positions, sizes, and numbers of the exhaust holes provided in the respective exhaust regions 220h so that the exhaust amounts from the respective exhaust regions 220h are approximately the same.

基板處理裝置10例如圖1所示,包括:控制部70,用以控制基板處理裝置10的各構成要素。控制部70亦可係包括CPU(Central Processing Unit;中央處理單元)等控制裝置、記憶體等記憶裝置、輸出輸入裝置等之電腦。控制部70藉由CPU隨著記憶體所記憶之控制程式運作,而控制基板處理裝置10的各構成要素。The substrate processing apparatus 10 includes, for example, a control unit 70 for controlling each component of the substrate processing apparatus 10 as shown in FIG. 1 . The control unit 70 may include a control device such as a CPU (Central Processing Unit), a memory device such as a memory, and a computer such as an input device. The control unit 70 controls each component of the substrate processing apparatus 10 by the CPU operating in accordance with a control program stored in the memory.

控制部70將控制載置台14的旋轉速度之控制訊號傳送至驅動裝置24。此外,控制部70將控制基板W的溫度之控制訊號傳送至加熱器26所連接之電源。此外,控制部70將控制前驅物氣體的流量之控制訊號傳送至閥161v~163v及流量控制器161c~163c。此外,控制部70將控制排氣口18a所連接之排氣裝置34的排氣量之控制訊號傳送至排氣裝置34。The control unit 70 transmits a control signal for controlling the rotational speed of the mounting table 14 to the drive device 24. Further, the control unit 70 transmits a control signal for controlling the temperature of the substrate W to the power source to which the heater 26 is connected. Further, the control unit 70 transmits a control signal for controlling the flow rate of the precursor gas to the valves 161v to 163v and the flow rate controllers 161c to 163c. Further, the control unit 70 transmits a control signal for controlling the amount of exhaust of the exhaust unit 34 to which the exhaust port 18a is connected to the exhaust unit 34.

此外,控制部70將控制沖洗氣體的流量之控制訊號傳送至閥20v及流量控制器20c。此外,控制部70將控制微波的傳送功率之控制訊號傳送至微波產生器68。此外,控制部70將控制反應氣體的流量之控制訊號傳送至閥50v、閥51v、流量控制部50c、及流量控制部51。此外,控制部70將控制來自排氣部22h的排氣量之控制訊號傳送至排氣裝置52。Further, the control unit 70 transmits a control signal for controlling the flow rate of the flushing gas to the valve 20v and the flow rate controller 20c. Further, the control unit 70 transmits a control signal for controlling the transmission power of the microwave to the microwave generator 68. Further, the control unit 70 transmits a control signal for controlling the flow rate of the reaction gas to the valve 50v, the valve 51v, the flow rate control unit 50c, and the flow rate control unit 51. Further, the control unit 70 transmits a control signal for controlling the amount of exhaust gas from the exhaust unit 22h to the exhaust unit 52.

藉由如同上述構成之基板處理裝置10,前驅物氣體從第一氣體供給部16噴射至基板W上,且藉由第二氣體供給部20而自基板W去除過度化學吸附之前驅物氣體。而且,基板W曝於由電漿產生部22而產生之反應氣體的電漿。基板處理裝置10對基板W重複上述運作,藉以在基板W形成既定厚度的膜。By the substrate processing apparatus 10 configured as described above, the precursor gas is ejected from the first gas supply unit 16 onto the substrate W, and the precursor gas is excessively chemisorbed from the substrate W by the second gas supply unit 20. Further, the substrate W is exposed to the plasma of the reaction gas generated by the plasma generating portion 22. The substrate processing apparatus 10 repeats the above operation on the substrate W, whereby a film having a predetermined thickness is formed on the substrate W.

於此,說明基板處理裝置10的實施例,即基板處理裝置10-1~10-3。圖7係顯示從上方觀察情形下之實施例1的基板處理裝置10-1的一範例之模式圖。圖8係顯示實施例1中的基板處理裝置10-1的一範例之剖面圖。圖8顯示圖7所示之基板處理裝置10-1之B-B剖面。Here, the substrate processing apparatuses 10-1 to 10-3, which are embodiments of the substrate processing apparatus 10, will be described. Fig. 7 is a schematic view showing an example of the substrate processing apparatus 10-1 of the first embodiment in the case of viewing from above. Fig. 8 is a cross-sectional view showing an example of the substrate processing apparatus 10-1 in the first embodiment. Fig. 8 shows a B-B cross section of the substrate processing apparatus 10-1 shown in Fig. 7.

實施例1之基板處理裝置10-1例如圖7所示,各天線22a在天線22a的區域內之靠近軸線X側具有三個內側噴射口50b。各個內側噴射口50b例如圖8所示,設在比天線22a的天板40的軸線X側的外緣更遠離軸線X的位置。各個內側噴射口50b例如如同圖8所示之箭號,朝往基板載置區域14a所載置的基板W之軸線X側的邊緣所通過之載置台14上的位置,將反應氣體噴射至斜下方。In the substrate processing apparatus 10-1 of the first embodiment, for example, as shown in FIG. 7, each antenna 22a has three inner injection ports 50b on the side closer to the axis X in the region of the antenna 22a. Each of the inner injection ports 50b is provided at a position farther from the axis X than the outer edge of the axis X side of the sun plate 40 of the antenna 22a, as shown in FIG. Each of the inner injection ports 50b, for example, has an arrow as shown in FIG. 8, and ejects the reaction gas to the position on the mounting table 14 through which the edge on the axis X side of the substrate W placed on the substrate mounting region 14a passes. Below.

此外,實施例1之基板處理裝置10-1例如圖7所示,各天線22a在天線22a區域內之遠離軸線X側具有三個的外側噴射口51b。各個外側噴射口51b例如圖8所示,設在比天線22a的天板40之遠離軸線X側的外緣更靠近軸線X的位置。各個外側噴射口51b例如如同圖8所示之箭號,朝往基板載置區域14a所載置的基板W之遠離軸線X側的邊緣所通過之載置台14上的位置,將反應氣體噴射至斜下方。此外,實施例1之基板處理裝置10-1之中,內側噴射口50b及外側噴射口51b例如圖8所示,係設在上部構件12b的內部。Further, in the substrate processing apparatus 10-1 of the first embodiment, as shown in FIG. 7, for example, each of the antennas 22a has three outer ejection openings 51b on the side far from the axis X in the region of the antenna 22a. Each of the outer injection ports 51b is provided at a position closer to the axis X than the outer edge of the sun plate 40 on the side of the axis X of the antenna 22a, as shown in FIG. Each of the outer injection ports 51b, for example, like an arrow shown in FIG. 8, sprays the reaction gas to a position on the mounting table 14 through which the edge of the substrate W placed on the substrate mounting region 14a passes away from the axis X side. Oblique below. Further, in the substrate processing apparatus 10-1 of the first embodiment, the inner injection port 50b and the outer injection port 51b are provided inside the upper member 12b as shown in Fig. 8, for example.

此外,實施例1之基板處理裝置10-1之中,例如圖7所示,沿著載置台14的周緣而設置排氣部22h的排氣區域220h。設有各天線22a之角度區域例如圖8所示,形成有多個排氣孔223的蓋部221係設在溝部222之上。排氣部22h在各個排氣區域220h之中,藉由排氣裝置52的運作,由設在蓋部221之多個排氣孔223經由溝部222而將處理室C內的氣體加以排氣。Further, in the substrate processing apparatus 10-1 of the first embodiment, as shown in FIG. 7, for example, the exhaust region 220h of the exhaust portion 22h is provided along the periphery of the mounting table 14. An angle region in which each antenna 22a is provided is, for example, as shown in FIG. 8, and a lid portion 221 in which a plurality of exhaust holes 223 are formed is provided on the groove portion 222. The exhaust unit 22h exhausts the gas in the processing chamber C through the plurality of exhaust holes 223 provided in the lid portion 221 through the groove portion 222 in the respective exhaust regions 220h by the operation of the exhaust device 52.

圖9係顯示從上方觀察情形下之實施例2的基板處理裝置10-2的一範例之模式圖。圖10係顯示實施例2之基板處理裝置10-2的一範例之剖面圖。圖10顯示圖9所示之基板處理裝置10-2之B-B剖面。Fig. 9 is a schematic view showing an example of the substrate processing apparatus 10-2 of the second embodiment in the case of viewing from above. Fig. 10 is a cross-sectional view showing an example of the substrate processing apparatus 10-2 of the second embodiment. Fig. 10 shows a B-B cross section of the substrate processing apparatus 10-2 shown in Fig. 9.

實施例2之基板處理裝置10-2例如圖9所示,各天線22a在比天線22a區域更靠近軸線X的位置具有三個內側噴射口50b。各個內側噴射口50b例如如同圖10所示之箭號,沿著載置台14的平面方向而將反應氣體噴射至脫離軸線X的方向。各個內側噴射口50b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行之方向。In the substrate processing apparatus 10-2 of the second embodiment, as shown in FIG. 9, for example, each of the antennas 22a has three inner injection ports 50b at a position closer to the axis X than the area of the antenna 22a. Each of the inner injection ports 50b, for example, like an arrow shown in FIG. 10, injects a reaction gas in a direction away from the axis X in the planar direction of the stage 14. Each of the inner injection ports 50b ejects, for example, a reaction gas into a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14.

此外,實施例2之基板處理裝置10-2例如圖9所示,各天線22a在比天線22a區域更遠離軸線X側具有75個外側噴射口51b。就各天線22a而言,設置外側噴射口51b的角度範圍係48°。各個外側噴射口51b例如如同圖10所示之箭號,沿著載置台14的平面方向而將反應氣體噴射至接近軸線X的方向。各個外側噴射口51b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之板W的面平行之方向。此外,實施例2之基板處理裝置10-2之中,例如圖10所示,內側噴射口50b及外側噴射口51b係作為與上部構件12b或天線22a有別之構件而安裝在上部構件12b的下部。藉此,能容易將內側噴射口50b及外側噴射口51b從上部構件12b或天線22a卸除,且內側噴射口50b及外側噴射口51b的維修變得容易。Further, in the substrate processing apparatus 10-2 of the second embodiment, as shown in FIG. 9, for example, each of the antennas 22a has 75 outer ejection openings 51b on the side farther from the axis X than the region of the antenna 22a. For each of the antennas 22a, the angle range in which the outer injection ports 51b are provided is 48°. Each of the outer injection ports 51b, for example, like an arrow shown in FIG. 10, injects a reaction gas in a direction close to the axis X along the plane direction of the stage 14. Each of the outer injection ports 51b ejects, for example, a reaction gas into a direction parallel to the surface of the plate W placed on the substrate placement region 14a of the mounting table 14. Further, in the substrate processing apparatus 10-2 of the second embodiment, as shown in FIG. 10, for example, the inner injection port 50b and the outer injection port 51b are attached to the upper member 12b as members other than the upper member 12b or the antenna 22a. Lower part. Thereby, the inner injection port 50b and the outer injection port 51b can be easily removed from the upper member 12b or the antenna 22a, and the maintenance of the inner injection port 50b and the outer injection port 51b becomes easy.

此外,實施例2之基板處理裝置10-2之中,例如圖9所示,沿著載置台14的周緣而設置排氣部22h的排氣區域220h。設有各天線22a之角度區域例如圖10所示,形成有多個排氣孔223的蓋部221係設在溝部222之上。實施例2之基板處理裝置10-2之中,在外側噴射口51b的下方設置排氣區域220h。排氣部22h在排氣區域220h之中,藉由排氣裝置52的運作,由蓋部221所設之多個排氣孔223經由溝部222而將處理室C內的氣體加以排氣。Further, in the substrate processing apparatus 10-2 of the second embodiment, as shown in FIG. 9, for example, the exhaust region 220h of the exhaust portion 22h is provided along the periphery of the mounting table 14. An angle region in which each antenna 22a is provided is, for example, as shown in FIG. 10, and a lid portion 221 in which a plurality of exhaust holes 223 are formed is provided on the groove portion 222. In the substrate processing apparatus 10-2 of the second embodiment, an exhaust region 220h is provided below the outer injection port 51b. In the exhaust portion 22h, in the exhaust region 220h, the gas in the processing chamber C is exhausted through the plurality of exhaust holes 223 provided in the lid portion 221 by the operation of the exhaust device 52 via the groove portion 222.

圖11係表示從上方觀察情形下之實施例3之基板處理裝置10-3的一範例之模式圖。圖12係表示實施例3之基板處理裝置10-3的一範例之剖面圖。圖12係表示圖11所示基板處理裝置10-3之B-B剖面。Fig. 11 is a schematic view showing an example of the substrate processing apparatus 10-3 of the third embodiment in the case of viewing from above. Fig. 12 is a cross-sectional view showing an example of the substrate processing apparatus 10-3 of the third embodiment. Fig. 12 is a cross-sectional view taken along line B-B of the substrate processing apparatus 10-3 shown in Fig. 11.

實施例3之基板處理裝置10-3例如圖11所示,各天線22a在比天線22a區域更接近軸線X的位置具有三個內側噴射口50b。各個內側噴射口50b例如圖12所示之箭號,沿著載置台14的平面方向而往脫離軸線X的方向噴射反應氣體。各個內側噴射口50b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行的方向。In the substrate processing apparatus 10-3 of the third embodiment, for example, as shown in FIG. 11, each of the antennas 22a has three inner injection ports 50b at a position closer to the axis X than the area of the antenna 22a. Each of the inner injection ports 50b, for example, an arrow shown in FIG. 12, ejects a reaction gas in a direction away from the axis X in the planar direction of the mounting table 14. Each of the inner injection ports 50b ejects, for example, a reaction gas into a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14.

此外,實施例3之基板處理裝置10-3例如圖11所示,各天線22a在比天線22a區域更遠離軸線X之側具有75個外側噴射口51b。就各天線22a而言,設置外側噴射口51b的角度範圍係48°。各個外側噴射口51b例如圖12所示之箭號,沿著載置台14的平面方向而往接近軸線X的方向噴射反應氣體。各個外側噴射口51b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行之方向。此外,即使於實施例3之基板處理裝置10-3之中,內側噴射口50b及外側噴射口51b例如圖12所示,亦作為與上部構件12b有別的構件而安裝在上部構件12b的下部。Further, in the substrate processing apparatus 10-3 of the third embodiment, as shown in FIG. 11, for example, each of the antennas 22a has 75 outer ejection openings 51b on the side farther from the axis X than the region of the antenna 22a. For each of the antennas 22a, the angle range in which the outer injection ports 51b are provided is 48°. Each of the outer injection ports 51b, for example, an arrow shown in FIG. 12, ejects a reaction gas in a direction approaching the axis X along the plane direction of the mounting table 14. Each of the outer injection ports 51b ejects, for example, a reaction gas into a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14. Further, even in the substrate processing apparatus 10-3 of the third embodiment, the inner injection port 50b and the outer injection port 51b are attached to the lower portion of the upper member 12b as a separate member from the upper member 12b, as shown in Fig. 12, for example. .

此外,實施例3之基板處理裝置10-3例如圖11所示,沿著載置台14的周緣而設置排氣部22h的排氣區域220h。排氣區域220h設置在係載置台14的周緣、且未設有天線22a的角度區域。此外,實施例3之基板處理裝置10-3之中,在係外側噴射口51b的下方且係蓋部221上設置間隔件220。間隔件220設在係載置台14的周緣、且係設有外側噴射口51b之48°的角度範圍,並具有與自蓋部221的頂面至載置台14的頂面之高度約略相同的厚度。間隔件220在外側噴射口51b的下方,抑制由載置台14的蓋部221之高低差而生之氣體流速的增加。Further, in the substrate processing apparatus 10-3 of the third embodiment, for example, as shown in FIG. 11, the exhaust region 220h of the exhaust portion 22h is provided along the periphery of the mounting table 14. The exhaust region 220h is provided on the peripheral edge of the mounting base 14, and the angular region where the antenna 22a is not provided. Further, in the substrate processing apparatus 10-3 of the third embodiment, the spacer 220 is provided below the outer ejection opening 51b and on the cap portion 221 . The spacer 220 is provided on the periphery of the mounting table 14 and has an angular range of 48° of the outer ejection opening 51b, and has a thickness substantially the same as the height from the top surface of the cover portion 221 to the top surface of the mounting table 14. . The spacer 220 suppresses an increase in the gas flow rate generated by the height difference of the lid portion 221 of the mounting table 14 below the outer injection port 51b.

圖13~圖18係顯示於實施例1~3將反應氣體的流量及RDC(Radical Distribution Control;自由基分佈控制)加以改變之情形下基板W上的膜厚分布之一範例。就各天線22a而言,RDC係以下述比率表示:即『從內側噴射口50b噴射之反應氣體的流量』,對於『從內側噴射口50b噴射之反應氣體的流量與從外側噴射口51b噴射之反應氣體的流量之合計流量』的比率。圖13~圖18之中,Y軸係表示在基板W的面上脫離軸線X的方向,Y軸中的0係表示基板W的中央。FIGS. 13 to 18 show an example of the film thickness distribution on the substrate W in the case where the flow rate of the reaction gas and the RDC (Radical Distribution Control) are changed in the first to third embodiments. In each of the antennas 22a, the RDC is expressed by the ratio "the flow rate of the reaction gas injected from the inner injection port 50b", and the flow rate of the reaction gas injected from the inner injection port 50b and the injection from the outer injection port 51b. The ratio of the total flow rate of the flow rate of the reaction gas. In FIGS. 13 to 18, the Y-axis indicates the direction in which the surface of the substrate W is separated from the axis X, and the 0 in the Y-axis indicates the center of the substrate W.

圖13顯示反應氣體的合計流量係630sccm、且RDC係0%之情形下基板W的膜厚分布。圖14顯示反應氣體的合計流量係630sccm、且RDC係100%之情形下基板W的膜厚分布。於圖13及圖14之實驗使用的反應氣體係NH3/H2/Ar的混合氣體,個別的流量係86/464/80sccm。Fig. 13 shows the film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 630 sccm and the RDC is 0%. Fig. 14 shows the film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 630 sccm and the RDC system is 100%. The mixed gas of the reaction gas system NH3/H2/Ar used in the experiments of Figs. 13 and 14 has an individual flow rate of 86/464/80 sccm.

圖15顯示反應氣體的合計流量係1730sccm、且RDC係0%之情形下基板W的膜厚分布。圖16係顯示反應氣體的合計流量係1730sccm、且RDC係100%之情形下基板W的膜厚分布。於圖15及圖16的實驗使用之反應氣體的流量比為NH3/H2/Ar=260/1390/80sccm。Fig. 15 shows a film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 1730 sccm and the RDC is 0%. Fig. 16 is a graph showing the film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 1730 sccm and the RDC system is 100%. The flow rate ratio of the reaction gas used in the experiments of Figs. 15 and 16 was NH3/H2/Ar = 260/1390 / 80 sccm.

圖17顯示反應氣體的合計流量係4830sccm、且RDC係0%之情形下基板W的膜厚分布。圖18顯示反應氣體的合計流量係4830sccm、且RDC係100%之情形下基板W的膜厚分布。於圖17及圖18的實驗使用之反應氣體的流量比為NH3/H2/Ar=750/4000/80sccm。Fig. 17 shows a film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 4830 sccm and the RDC is 0%. Fig. 18 shows a film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 4830 sccm and the RDC system is 100%. The flow rate ratio of the reaction gas used in the experiments of Figs. 17 and 18 was NH3/H2/Ar = 750/4000/80 sccm.

當參照圖13、圖15、及圖17時,則RDC係0%之情形下,亦即已僅從外側噴射口51b噴射反應氣體之情形下,實施例2及實施例3相較於實施例1,G/R(Growth Rate;成長率)更低。因為實施例1相較於實施例2及實施例3,外側噴射口51b的數量更少,所以已噴射相同流量的反應氣體之情形下,實施例1之反應氣體的流速亦較快。因此,吾人認為,實施例1之中,大量的已從外側噴射口51b噴射之反應氣體,流動向脫離載置台14的周緣所設之排氣部22h的方向,且即使相較於實施例2及實施例3,反應氣體流動在基板W上的量變更多。然而,當流動在基板W上之反應氣體的流速過快時,則反應氣體的元素無法充分解離在基板W上,基板W上所形成之膜的品質變得不佳。基板W所形成之膜的品質能例如使用WERR(Wet Etching Rate Ratio;濕式蝕刻速率比例)而評估。Referring to Fig. 13, Fig. 15, and Fig. 17, in the case where the RDC is 0%, that is, in the case where the reaction gas has been ejected only from the outer ejection port 51b, the embodiment 2 and the embodiment 3 are compared with the embodiment. 1, G / R (Growth Rate; growth rate) is lower. Since the number of the outer injection ports 51b is smaller than that of the second embodiment and the third embodiment, the flow rate of the reaction gas of the first embodiment is also faster in the case where the reaction gas of the same flow rate has been injected. Therefore, in the first embodiment, a large amount of the reaction gas injected from the outer injection port 51b flows in the direction away from the exhaust portion 22h provided on the periphery of the mounting table 14, and even in comparison with the second embodiment And in Example 3, the amount of the reaction gas flowing on the substrate W became larger. However, when the flow rate of the reaction gas flowing on the substrate W is too fast, the elements of the reaction gas are not sufficiently dissociated on the substrate W, and the quality of the film formed on the substrate W becomes poor. The quality of the film formed by the substrate W can be evaluated, for example, using WERP (Wet Etching Rate Ratio).

另一方面,因為實施例2及實施例3相較於實施例1而外側噴射口51b的數量更多,所以已噴射與實施例1相同流量的反應氣體之情形下,相較於實施例1,反應氣體的流速更慢。因此,實施例2及實施例3之中,可期待基板W上所形成之膜的品質之提昇。然而,實施例2及實施例3因為反應氣體的流速慢、且外側噴射口51b的附近設有排氣區域220h,所以大量的已從外側噴射口51b噴射之反應氣體會流入排氣區域220h。因此,吾人認為實施例2及實施例3之中,流動在基板W上之反應氣體的數量減少,且相較於實施例1,G/R更降低。On the other hand, since the number of the outer injection ports 51b is larger than that of the first embodiment and the third embodiment, the reaction gas having the same flow rate as that of the first embodiment has been injected, compared to the first embodiment. The flow rate of the reaction gas is slower. Therefore, in the second and third embodiments, the quality of the film formed on the substrate W can be expected to be improved. However, in the second and third embodiments, since the flow rate of the reaction gas is slow and the exhaust region 220h is provided in the vicinity of the outer injection port 51b, a large amount of the reaction gas that has been injected from the outer injection port 51b flows into the exhaust region 220h. Therefore, it is considered that in Example 2 and Example 3, the amount of the reaction gas flowing on the substrate W is decreased, and G/R is lower than that in the first embodiment.

其中,實施例2如同圖9及圖10所說明,在載置台14的周緣,外側噴射口51b的下方設有排氣區域220h,但實施例3如同圖11及圖12所說明,在載置台14的周緣,配置有外側噴射口51b之角度區域未設有排氣區域220h、而未配置外側噴射口51b之角度區域設有排氣區域220h。因此,吾人認為,實施例3之中,已從外側噴射口51b噴射之反應氣體於天線22a的底面與基板W的頂面之間的空間漂浮之時間比實施例2更長,且相較於實施例2,G/R更增加。如上所述,能利用改變外側噴射口51b與排氣區域220h之位置關係,而改變G/R。再者,吾人認為即使於實施例3,能利用削減外側噴射口51b的數量,提升從各個外側噴射口51b噴射之反應氣體的流速,而增加往基板W上流動之反應氣體的量,且使G/R增加。In the second embodiment, as shown in FIG. 9 and FIG. 10, the exhaust region 220h is provided below the outer injection port 51b on the periphery of the mounting table 14, but the third embodiment is as shown in FIGS. 11 and 12, and is placed on the mounting table. In the peripheral edge of the 14th, the angular region in which the outer injection port 51b is disposed is not provided with the exhaust region 220h, and the angular region in which the outer injection port 51b is not disposed is provided with the exhaust region 220h. Therefore, it is considered that, in the third embodiment, the time during which the reaction gas injected from the outer ejection opening 51b floats in the space between the bottom surface of the antenna 22a and the top surface of the substrate W is longer than that of the second embodiment, and is compared with the second embodiment. In Example 2, G/R is further increased. As described above, it is possible to change the G/R by changing the positional relationship between the outer injection port 51b and the exhaust region 220h. Furthermore, in the third embodiment, it is considered that the flow rate of the reaction gas injected from each of the outer injection ports 51b can be increased by increasing the number of the outer injection ports 51b, and the amount of the reaction gas flowing on the substrate W can be increased. G/R increases.

此外,當將圖13、圖15、圖17、圖14、圖16、圖18加以比較時,RDC係0%則靠近外側噴射口51b之基板W的膜厚大,RDC係100%則靠近內側噴射口50b之基板W的膜厚大。而且,當參照圖13~18時,則實施例2及實施例3相較於實施例1,膜厚分布的梯度更大。如上所述,實施例2及實施例3比實施例1更提昇基板W的膜厚分布的控制性。Further, when comparing Fig. 13, Fig. 15, Fig. 17, Fig. 14, Fig. 16, and Fig. 18, the RDC is 0%, the thickness of the substrate W close to the outer ejection opening 51b is large, and the RDC is 100% closer to the inner side. The thickness of the substrate W of the ejection port 50b is large. Further, referring to Figs. 13 to 18, in Example 2 and Example 3, the gradient of the film thickness distribution was larger than that in Example 1. As described above, in the second and third embodiments, the controllability of the film thickness distribution of the substrate W is improved.

其次,說明相較於實施例3,更削減外側噴射口51b的數量之情形下的實驗結果。圖19係顯示從上方觀察情形下之實施例4的基板處理裝置10-4的一範例之模式圖。因為實施例4之基板處理裝置10-4的B-B剖面與圖12同樣,所以省略詳細說明。Next, an experimental result in the case where the number of the outer injection ports 51b is further reduced as compared with the third embodiment will be described. Fig. 19 is a schematic view showing an example of the substrate processing apparatus 10-4 of the fourth embodiment in the case of viewing from above. Since the B-B cross section of the substrate processing apparatus 10-4 of the fourth embodiment is the same as that of FIG. 12, detailed description thereof will be omitted.

實施例4之基板處理裝置10-4例如圖19所示,各天線22a在比天線22a區域更接近軸線X的位置具有三個內側噴射口50b。各個內側噴射口50b例如圖12所示之箭號,沿著載置台14的平面方向而往脫離軸線X的方向噴射反應氣體。各個內側噴射口50b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行的方向。In the substrate processing apparatus 10-4 of the fourth embodiment, as shown in FIG. 19, for example, each of the antennas 22a has three inner injection ports 50b at a position closer to the axis X than the region of the antenna 22a. Each of the inner injection ports 50b, for example, an arrow shown in FIG. 12, ejects a reaction gas in a direction away from the axis X in the planar direction of the mounting table 14. Each of the inner injection ports 50b ejects, for example, a reaction gas into a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14.

此外,實施例4之基板處理裝置10-4例如圖19所示,各天線22a在比天線22a區域更遠離軸線X之側具有37個外側噴射口51b。實施例4之中,各天線22a設置外側噴射口51b的角度範圍係24°。各個外側噴射口51b例如圖12所示之箭號,沿著載置台14的平面方向而往接近軸線X的方向噴射反應氣體。各個外側噴射口51b例如將反應氣體噴射至與載置台14的基板載置區域14a所載置之基板W的面平行的方向。Further, in the substrate processing apparatus 10-4 of the fourth embodiment, as shown in FIG. 19, each of the antennas 22a has 37 outer ejection openings 51b on the side farther from the axis X than the region of the antenna 22a. In the fourth embodiment, each of the antennas 22a is provided with an outer injection port 51b having an angular range of 24°. Each of the outer injection ports 51b, for example, an arrow shown in FIG. 12, ejects a reaction gas in a direction approaching the axis X along the plane direction of the mounting table 14. Each of the outer injection ports 51b ejects the reaction gas to a direction parallel to the surface of the substrate W placed on the substrate placement region 14a of the mounting table 14, for example.

此外,實施例4之基板處理裝置10-4例如圖19所示,沿著載置台14的周緣而設置排氣部22h的排氣區域220h。排氣區域220h設在係載置台14的周緣、且係未設有天線22a的角度區域。此外,實施例4之基板處理裝置10-4之中,外側噴射口51b的下方所設之間隔件220,設置在係載置台14的周緣、且係設有外側噴射口51b之24°的角度範圍。Further, in the substrate processing apparatus 10-4 of the fourth embodiment, for example, as shown in FIG. 19, the exhaust region 220h of the exhaust portion 22h is provided along the periphery of the mounting table 14. The exhaust region 220h is provided on the periphery of the mounting platform 14 and is an angular region in which the antenna 22a is not provided. Further, in the substrate processing apparatus 10-4 of the fourth embodiment, the spacer 220 provided below the outer ejection opening 51b is provided on the peripheral edge of the mounting base 14 and has an angle of 24° of the outer ejection opening 51b. range.

圖20~圖25顯示於實施例1、實施例4、及實施例5之中將反應氣體的流量加以改變之情形下基板上的膜厚分布的一範例。實施例5之基板處理裝置10的構成係使用圖1~圖6而說明之基板處理裝置10。圖20顯示反應氣體的合計流量係630sccm、且RDC係0%之情形下基板W的膜厚分布。於圖20的實驗使用之反應氣體的流量比為NH3/H2/Ar=86/464/80sccm。圖21係圖20的虛線部分的放大圖。20 to 25 show an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas is changed in the first embodiment, the fourth embodiment, and the fifth embodiment. The configuration of the substrate processing apparatus 10 of the fifth embodiment is the substrate processing apparatus 10 described with reference to FIGS. 1 to 6 . 20 shows the film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 630 sccm and the RDC is 0%. The flow rate of the reaction gas used in the experiment of Fig. 20 was NH3/H2/Ar = 86/464/80 sccm. Figure 21 is an enlarged view of a broken line portion of Figure 20.

圖22顯示反應氣體的合計流量係1650sccm、且RDC係0%之情形下基板W的膜厚分布。於圖22的實驗使用之反應氣體的流量比為NH3/H2=260/1390sccm。圖23係圖22的虛線部分的放大圖。Fig. 22 shows the film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 1650 sccm and the RDC is 0%. The flow rate of the reaction gas used in the experiment of Fig. 22 was NH3/H2 = 260/1390 sccm. Figure 23 is an enlarged view of a broken line portion of Figure 22.

圖24顯示反應氣體的合計流量係4750sccm、且RDC係0%之情形下基板W的膜厚分布。於圖24的實驗使用之反應氣體的流量比為NH3/H2=750/4000sccm。圖25係圖24的虛線部分的放大圖。Fig. 24 shows the film thickness distribution of the substrate W in the case where the total flow rate of the reaction gas is 4,750 sccm and the RDC is 0%. The flow rate of the reaction gas used in the experiment of Fig. 24 was NH3/H2 = 750 / 4000 sccm. Figure 25 is an enlarged view of a broken line portion of Figure 24.

當參照圖20~圖25時,則就各個天線22a而言,外側噴射口51b的數量削減至37個之實施例4及實施例5之中,G/R增加至與實施例1同樣程度。吾人認為,實施例4及實施例5藉由將外側噴射口51b削減至37個,而從各個外側噴射口51b噴射之反應氣體的流速加快,流通在基板W上之反應氣體的量變多。其中,實施例4及實施例5之中外側噴射口51b係37個,實施例1之中外側噴射口51b係三個。因此,實施例4及實施例5之中,從各個外側噴射口51b噴射之反應氣體的流速,慢於實施例1之中從各個外側噴射口51b噴射之反應氣體的流速。因此,實施例4及實施例5與實施例1相較,反應氣體於天線22a的底面與基板W的頂面之間的空間漂浮的時間變長,且反應氣體的元素解離的機率上昇。因此,實施例4及實施例5能使形成在基板W的膜的品質提昇。In the case of the antennas 22a, the number of the outer injection ports 51b is reduced to 37 in the fourth embodiment and the fifth embodiment, and the G/R is increased to the same level as in the first embodiment. In the fourth and fifth embodiments, the flow rate of the reaction gas ejected from each of the outer injection ports 51b is increased, and the amount of the reaction gas flowing through the substrate W is increased. In the fourth and fifth embodiments, there are 37 outer injection ports 51b, and in the first embodiment, the outer injection ports 51b are three. Therefore, in the fourth and fifth embodiments, the flow velocity of the reaction gas injected from each of the outer injection ports 51b is slower than the flow velocity of the reaction gas injected from the respective outer injection ports 51b in the first embodiment. Therefore, in the fourth and fifth embodiments, the time during which the reaction gas floats in the space between the bottom surface of the antenna 22a and the top surface of the substrate W becomes longer as compared with the first embodiment, and the probability of elemental dissociation of the reaction gas increases. Therefore, in the fourth embodiment and the fifth embodiment, the quality of the film formed on the substrate W can be improved.

此外,當參照圖21、圖23、及圖25時,則實施例1之中,伴隨反應氣體的流量增加,外側噴射口51b側的之基板W的邊緣附近的G/R比基板W上之其他區域的G/R更相對降低。吾人認為,此係因為伴隨反應氣體的流量之增加而從各個外側噴射口51b噴射之反應氣體的流速上昇,且大量的反應氣體會流動向軸線X側,外側噴射口51b側之基板W的邊緣附近的反應氣體的濃度相對降低。Further, referring to Fig. 21, Fig. 23, and Fig. 25, in the first embodiment, as the flow rate of the reaction gas increases, the G/R in the vicinity of the edge of the substrate W on the side of the outer ejection opening 51b is larger than that on the substrate W. The G/R of other areas is relatively lower. In the present invention, the flow rate of the reaction gas ejected from each of the outer injection ports 51b increases as the flow rate of the reaction gas increases, and a large amount of the reaction gas flows toward the axis X side and the edge of the substrate W on the side of the outer injection port 51b. The concentration of the nearby reaction gas is relatively lowered.

相較於此,實施例4之中反應氣體的流量增加之情形下,在外側噴射口51b側的基板W的邊緣附近,G/R之增長減緩,但不見G/R相對降低。此外,實施例5之中反應氣體的流量即使增加,在外側噴射口51b側的基板W的邊緣附近亦不見G/R相對降低、且亦不見G/R之增長的減緩。吾人認為,此係因為實施例4及實施例5相較於實施例1,外側噴射口51b的數量更多,且相對於反應氣體的流量,流速的增加量更低。此外,實施例5係比實施例4在更廣的角度範圍分散配置有多個外側噴射口51b,因此相較於緊密配置有多個外側噴射口51b之實施例4,從多個外側噴射口51b噴射之反應氣體之流速的降低更快。因此,吾人認為,實施例5相較於實施例4,更抑制到達基板W上之反應氣體的流速,並更高程度保持反應氣體之元素解離的機率。On the other hand, in the case where the flow rate of the reaction gas in the fourth embodiment is increased, the growth of G/R is slowed in the vicinity of the edge of the substrate W on the side of the outer ejection opening 51b, but the relative decrease in G/R is not observed. Further, even if the flow rate of the reaction gas in the fifth embodiment is increased, the G/R is not decreased in the vicinity of the edge of the substrate W on the side of the outer injection port 51b, and the increase in the G/R is not observed. It is considered that this is because the number of the outer injection ports 51b is larger than that of the first embodiment and the fifth embodiment, and the amount of increase in the flow rate is lower with respect to the flow rate of the reaction gas. Further, in the fifth embodiment, a plurality of outer injection ports 51b are disposed in a wider angular range than in the fourth embodiment, and therefore, from the plurality of outer injection ports, the fourth embodiment is provided in comparison with the fourth embodiment in which the plurality of outer injection ports 51b are closely arranged. The decrease in the flow rate of the reaction gas injected by 51b is faster. Therefore, it is considered that Example 5 suppresses the flow rate of the reaction gas reaching the substrate W and maintains the probability of elemental dissociation of the reaction gas to a higher degree than that of the embodiment 4.

以上已說明本發明之一實施形態。依據本實施形態之基板處理裝置10,能使自載置台14的旋轉中心至載置台14的徑向之基板W上的膜厚分布之控制性提昇。An embodiment of the present invention has been described above. According to the substrate processing apparatus 10 of the present embodiment, the controllability of the film thickness distribution on the substrate W from the rotation center of the mounting table 14 to the radial direction of the mounting table 14 can be improved.

另外,上述實施形態之中,就基板處理裝置10而言,以使用PE-ALD法而在基板W上形成既定的膜之成膜裝置為例說明,但本發明揭示的技術不限於此。例如,上述實施形態所揭示的技術,只要係對基板W而將使用反應氣體的電漿之處理加以施行的裝置,亦能運用在電漿蝕刻裝置(例如ALE(Atomic Layer Etching;原子層蝕刻)裝置等)、將使用電漿之改質處理加以施行的裝置等。In the above-described embodiment, the substrate processing apparatus 10 is described as an example of a film forming apparatus that forms a predetermined film on the substrate W by the PE-ALD method. However, the technology disclosed in the present invention is not limited thereto. For example, the technique disclosed in the above embodiments can be applied to a plasma etching apparatus (for example, ALE (Atomic Layer Etching)) as long as the processing of the plasma using the reactive gas is performed on the substrate W. A device or the like which is to be subjected to a plasma modification treatment.

依據上述內容,應理解本案之各種實施例係為了說明而記載,且能不超脫本案的範圍及精神而施行各類變形。從而,於此揭示之各種實施例非用以限制接下來的各請求項所指定之本質性範圍及精神。Based on the above, it should be understood that the various embodiments of the present invention are described for the purpose of illustration, and various modifications may be made without departing from the scope and spirit of the invention. Accordingly, the various embodiments disclosed herein are not intended to limit the scope and spirit of the inventions.

10‧‧‧基板處理裝置
10-1~10-3‧‧‧基板處理裝置
12‧‧‧處理容器
12a‧‧‧下部構件
12b‧‧‧上部構件
12q‧‧‧排氣道
12r‧‧‧氣體供給道
14‧‧‧載置台
14a‧‧‧基板載置區域
16‧‧‧第一氣體供給部
16a‧‧‧噴射部
16h‧‧‧噴射口
18‧‧‧排氣部
18a‧‧‧排氣口
18d‧‧‧空間
18g‧‧‧間隙
18q‧‧‧排氣道
20‧‧‧第二氣體供給部
20a‧‧‧噴射口
20c‧‧‧流量控制器
20d‧‧‧空間
20g‧‧‧氣體供給源
20p‧‧‧間隙
20r‧‧‧氣體供給道
20v‧‧‧閥
22‧‧‧電漿產生部
22a‧‧‧天線
22b‧‧‧同軸導波管
22c‧‧‧反應氣體供給部
22h‧‧‧排氣部
24‧‧‧驅動機構
24a‧‧‧驅動裝置
24b‧‧‧旋轉軸
26‧‧‧加熱器
34‧‧‧排氣裝置
40‧‧‧天板
42‧‧‧槽孔板
44‧‧‧慢波板
46‧‧‧冷卻板
50b‧‧‧內側噴射口
50c‧‧‧流量控制部
50g‧‧‧氣體供給源
50v‧‧‧閥
51b‧‧‧外側噴射口
51c‧‧‧流量控制部
51v‧‧‧閥
52‧‧‧排氣裝置
60‧‧‧導波管
62a‧‧‧內側導體
62b‧‧‧外側導體
68‧‧‧微波產失器
70‧‧‧控制部
121p~123p‧‧‧氣體供給道
161‧‧‧內側氣體供給部
161a‧‧‧內側噴射部
161b‧‧‧彈性構件
161c‧‧‧流量控制器
161d‧‧‧緩衝空間
161p‧‧‧氣體供給道
161v‧‧‧閥
162‧‧‧中間氣體供給部
162a‧‧‧內側噴射部
162b‧‧‧彈性構件
162c‧‧‧流量控制器
162d‧‧‧緩衝空間
162p‧‧‧氣體供給道
162v‧‧‧閥
163‧‧‧外側氣體供給部
163a‧‧‧內側噴射部
163b‧‧‧彈性構件
163c‧‧‧流量控制器
163d‧‧‧緩衝空間
163p‧‧‧氣體供給道
163v‧‧‧閥
220‧‧‧間隔件
220h‧‧‧排氣區域
221‧‧‧蓋部
222‧‧‧溝部
223‧‧‧排氣孔
A1‧‧‧內側環狀區域
A2‧‧‧中間環狀區域
A3‧‧‧外側環狀區域
AP‧‧‧開口
C‧‧‧處理室
G‧‧‧閘閥
L‧‧‧長度
M1~M4‧‧‧第一構件~第四構件
r1~r4‧‧‧距離
R1‧‧‧第一區域
R2‧‧‧第二區域
U‧‧‧單元
W‧‧‧晶圓
W1‧‧‧直徑
X‧‧‧軸線
Y‧‧‧軸線
10‧‧‧Substrate processing unit
10-1~10-3‧‧‧Substrate processing device
12‧‧‧Processing container
12a‧‧‧lower components
12b‧‧‧ upper member
12q‧‧‧ exhaust duct
12r‧‧‧ gas supply road
14‧‧‧ mounting table
14a‧‧‧Substrate placement area
16‧‧‧First Gas Supply Department
16a‧‧‧Injection Department
16h‧‧‧jet
18‧‧‧Exhaust Department
18a‧‧‧Exhaust port
18d‧‧‧ space
18g‧‧‧ gap
18q‧‧‧ exhaust duct
20‧‧‧Second Gas Supply Department
20a‧‧‧jet
20c‧‧‧Flow Controller
20d‧‧‧ space
20g‧‧‧ gas supply source
20p‧‧‧ gap
20r‧‧‧ gas supply road
20v‧‧‧ valve
22‧‧‧ Plasma Production Department
22a‧‧‧Antenna
22b‧‧‧ coaxial waveguide
22c‧‧‧Reactive Gas Supply Department
22h‧‧‧Exhaust Department
24‧‧‧ drive mechanism
24a‧‧‧ drive
24b‧‧‧Rotary axis
26‧‧‧heater
34‧‧‧Exhaust device
40‧‧‧天板
42‧‧‧Slot plate
44‧‧‧ Slow wave board
46‧‧‧Cooling plate
50b‧‧‧Inside injection port
50c‧‧‧Flow Control Department
50g‧‧‧ gas supply source
50v‧‧‧ valve
51b‧‧‧Outer jet
51c‧‧‧Flow Control Department
51v‧‧‧ valve
52‧‧‧Exhaust device
60‧‧‧waveguide
62a‧‧‧Inside conductor
62b‧‧‧Outer conductor
68‧‧‧Microwave Loss
70‧‧‧Control Department
121p~123p‧‧‧ gas supply road
161‧‧‧Internal Gas Supply Department
161a‧‧‧Inside Jetting Department
161b‧‧‧Flexible components
161c‧‧‧Flow Controller
161d‧‧‧ buffer space
161p‧‧‧ gas supply road
161v‧‧‧ valve
162‧‧‧Intermediate Gas Supply Department
162a‧‧‧Inside Jetting Department
162b‧‧‧Flexible components
162c‧‧‧Flow Controller
162d‧‧‧ buffer space
162p‧‧‧ gas supply road
162v‧‧‧ valve
163‧‧‧Outside Gas Supply Department
163a‧‧‧Inside Jetting Department
163b‧‧‧Flexible components
163c‧‧‧Flow Controller
163d‧‧‧ buffer space
163p‧‧‧ gas supply road
163v‧‧‧ valve
220‧‧‧ spacers
220h‧‧‧Exhaust area
221‧‧‧ 盖部
222‧‧‧Ditch
223‧‧‧ venting holes
A1‧‧‧inside annular zone
A2‧‧‧ intermediate ring zone
A3‧‧‧Outer annular area
AP‧‧‧ openings
C‧‧‧Processing room
G‧‧‧ gate valve
L‧‧‧ length
M1~M4‧‧‧first member to fourth member
R1~r4‧‧‧distance
R1‧‧‧ first area
R2‧‧‧ second area
Unit U‧‧‧
W‧‧‧ wafer
W1‧‧‧ diameter
X‧‧‧ axis
Y‧‧‧ axis

圖1係顯示基板處理裝置的一範例之剖面圖。1 is a cross-sectional view showing an example of a substrate processing apparatus.

圖2係顯示從上方觀察情形下之基板處理裝置的一範例之模式圖。Fig. 2 is a schematic view showing an example of a substrate processing apparatus in a case where it is viewed from above.

圖3係顯示圖1中的軸線X之左側部分的一範例之放大剖面圖。Fig. 3 is an enlarged cross-sectional view showing an example of the left side portion of the axis X in Fig. 1.

圖4係顯示圖1中的軸線X之左側部分的一範例之放大剖面圖。Fig. 4 is an enlarged cross-sectional view showing an example of a left side portion of the axis X in Fig. 1.

圖5顯示單元U的底面的一範例。Figure 5 shows an example of the bottom surface of unit U.

圖6係顯示圖1中的軸線X之右側部分的一範例之放大剖面圖。Fig. 6 is an enlarged cross-sectional view showing an example of a right portion of the axis X in Fig. 1.

圖7係顯示從上方觀察情形下之實施例1之基板處理裝置的一範例之模式圖。Fig. 7 is a schematic view showing an example of the substrate processing apparatus of the first embodiment in the case of viewing from above.

圖8係顯示實施例1中的基板處理裝置的一範例之剖面圖。Fig. 8 is a cross-sectional view showing an example of the substrate processing apparatus in the first embodiment.

圖9係顯示從上方觀察情形下之實施例2之基板處理裝置的一範例之模式圖。Fig. 9 is a schematic view showing an example of the substrate processing apparatus of the second embodiment in the case of viewing from above.

圖10係顯示實施例2中的基板處理裝置的一範例之剖面圖。Fig. 10 is a cross-sectional view showing an example of the substrate processing apparatus in the second embodiment.

圖11係顯示從上方觀察情形下之實施例3的基板處理裝置的一範例之模式圖。Fig. 11 is a schematic view showing an example of the substrate processing apparatus of the third embodiment in the case of viewing from above.

圖12係顯示實施例3中的基板處理裝置的一範例之剖面圖。Fig. 12 is a cross-sectional view showing an example of the substrate processing apparatus in the third embodiment.

圖13顯示實施例1~3中改變反應氣體的流量及RDC(Radical Distribution Control;自由基分佈控制)之情形下基板上的膜厚分布之一範例。Fig. 13 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC (Radical Distribution Control) were changed in Examples 1 to 3.

圖14顯示實施例1~3中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 14 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC were changed in Examples 1 to 3.

圖15顯示實施例1~3中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 15 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC were changed in Examples 1 to 3.

圖16顯示實施例1~3中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 16 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC were changed in Examples 1 to 3.

圖17顯示實施例1~3中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 17 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC were changed in Examples 1 to 3.

圖18顯示實施例1~3中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 18 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC were changed in Examples 1 to 3.

圖19係顯示從上方觀察情形下之實施例4的基板處理裝置的一範例之模式圖。Fig. 19 is a schematic view showing an example of the substrate processing apparatus of the fourth embodiment in the case of viewing from above.

圖20顯示實施例1、實施例4、及實施例5中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 20 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC are changed in the embodiment 1, the embodiment 4, and the embodiment 5.

圖21係圖20的虛線部分的放大圖。Figure 21 is an enlarged view of a broken line portion of Figure 20.

圖22顯示實施例1、實施例4、及實施例5中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 22 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC are changed in the first embodiment, the fourth embodiment, and the fifth embodiment.

圖23係圖22的虛線部分的放大圖。Figure 23 is an enlarged view of a broken line portion of Figure 22.

圖24顯示實施例1、實施例4、及實施例5中改變反應氣體的流量及RDC之情形下基板上的膜厚分布之一範例。Fig. 24 shows an example of the film thickness distribution on the substrate in the case where the flow rate of the reaction gas and the RDC were changed in Example 1, Example 4, and Example 5.

圖25係圖24的虛線部分的放大圖。Figure 25 is an enlarged view of a broken line portion of Figure 24.

10‧‧‧基板處理裝置 10‧‧‧Substrate processing unit

12‧‧‧處理容器 12‧‧‧Processing container

12a‧‧‧下部構件 12a‧‧‧lower components

12b‧‧‧上部構件 12b‧‧‧ upper member

12q‧‧‧排氣道 12q‧‧‧ exhaust duct

12r‧‧‧氣體供給道 12r‧‧‧ gas supply road

14‧‧‧載置台 14‧‧‧ mounting table

14a‧‧‧基板載置區域 14a‧‧‧Substrate placement area

16a‧‧‧噴射部 16a‧‧‧Injection Department

16h‧‧‧噴射口 16h‧‧‧jet

18‧‧‧排氣部 18‧‧‧Exhaust Department

18a‧‧‧排氣口 18a‧‧‧Exhaust port

20‧‧‧第二氣體供給部 20‧‧‧Second Gas Supply Department

20a‧‧‧噴射口 20a‧‧‧jet

22‧‧‧電漿產生部 22‧‧‧The Plasma Generation Department

22a‧‧‧天線 22a‧‧‧Antenna

22b‧‧‧同軸導波管 22b‧‧‧ coaxial waveguide

22c‧‧‧反應氣體供給部 22c‧‧‧Reactive Gas Supply Department

22h‧‧‧排氣部 22h‧‧‧Exhaust Department

24‧‧‧驅動機構 24‧‧‧ drive mechanism

24a‧‧‧驅動裝置 24a‧‧‧ drive

24b‧‧‧旋轉軸 24b‧‧‧Rotary axis

26‧‧‧加熱器 26‧‧‧heater

34‧‧‧排氣裝置 34‧‧‧Exhaust device

60‧‧‧導波管 60‧‧‧waveguide

68‧‧‧微波產失器 68‧‧‧Microwave Loss

70‧‧‧控制部 70‧‧‧Control Department

161‧‧‧內側氣體供給部 161‧‧‧Internal Gas Supply Department

162‧‧‧中間氣體供給部 162‧‧‧Intermediate Gas Supply Department

163‧‧‧外側氣體供給部 163‧‧‧Outside Gas Supply Department

AP‧‧‧開口 AP‧‧‧ openings

R2‧‧‧第二區域 R2‧‧‧ second area

X‧‧‧軸線 X‧‧‧ axis

Claims (8)

一種基板處理裝置,包括: 載置台,載置被處理基板,且設置成能以一軸線為中心旋轉,以使該被處理基板在該軸線的周圍移動; 天線,設在一電漿處理區域,該電漿處理區域係因該載置台之旋轉而在該軸線的周向移動之該被處理基板所依序通過的多個區域之中的一個區域;以及 氣體供給部,將反應氣體供給至該電漿處理區域; 且該氣體供給部具有: 內側噴射口,從該軸線方向觀察之情形下,係設在比該天線更靠近該軸線的位置,且往遠離該軸線之方向噴射反應氣體;以及 外側噴射口,從該軸線方向觀察之情形下,係設在比該天線更遠離該軸線的位置,且往接近該軸線之方向噴射反應氣體,此反應氣體的流量與從該內側噴射口噴射之反應氣體的流量係受到獨立控制。A substrate processing apparatus comprising: a mounting table on which a substrate to be processed is placed, and is arranged to be rotatable about an axis to move the substrate to be processed around the axis; and the antenna is disposed in a plasma processing region The plasma processing region is one of a plurality of regions sequentially passing through the substrate to be processed in the circumferential direction of the axis due to the rotation of the mounting table; and the gas supply portion supplies the reaction gas to the region a plasma processing region; and the gas supply portion has: an inner injection port, which is disposed closer to the axis than the antenna when viewed from the axial direction, and ejects the reaction gas away from the axis; The outer injection port is disposed at a position farther from the axis than the antenna when viewed from the axial direction, and ejects a reaction gas toward the axis, and the flow rate of the reaction gas is ejected from the inner injection port. The flow rate of the reaction gas is independently controlled. 如申請專利範圍第1項之基板處理裝置,其中, 從該軸線方向觀察之情形下,該內側噴射口及該外側噴射口將反應氣體朝向設有該天線之區域噴射。The substrate processing apparatus according to claim 1, wherein the inner injection port and the outer injection port eject the reaction gas toward a region where the antenna is provided, as viewed in the axial direction. 如申請專利範圍第1項之基板處理裝置,其中, 該內側噴射口及該外側噴射口,將反應氣體朝向與該載置台所載置之該被處理基板的面平行之方向噴射。The substrate processing apparatus according to claim 1, wherein the inner injection port and the outer injection port spray the reaction gas in a direction parallel to a surface of the substrate to be processed placed on the mounting table. 如申請專利範圍第1項之基板處理裝置,其中, 該氣體供給部具有多個該內側噴射口及該外側噴射口。The substrate processing apparatus according to claim 1, wherein the gas supply unit has a plurality of the inner injection ports and the outer injection ports. 如申請專利範圍第1項之基板處理裝置,其中, 在該電漿處理區域設有多數之該天線, 該內側噴射口及該外側噴射口,係對每一該天線分別分配一個以上,且對每一該天線噴射之反應氣體的流量可受到獨立控制。The substrate processing apparatus according to claim 1, wherein a plurality of the antennas are provided in the plasma processing region, and the inner injection port and the outer injection port are respectively assigned one or more to each of the antennas, and The flow rate of the reaction gas injected by each of the antennas can be independently controlled. 如申請專利範圍第1項之基板處理裝置,其中, 更包括:排氣區域,係沿著該載置台的周緣設置,且由多個排氣孔進行排氣; 從該軸線方向觀察之情形下,該多個排氣孔係設在與設有該天線之角度的區域不同之角度的區域。The substrate processing apparatus of claim 1, further comprising: an exhaust region disposed along a circumference of the mounting table and exhausted by the plurality of exhaust holes; and viewed from the axial direction The plurality of exhaust holes are provided at an angle different from a region where the angle of the antenna is provided. 如申請專利範圍第6項之基板處理裝置,其中, 沿著該載置台的周緣設置多個該排氣區域。A substrate processing apparatus according to claim 6, wherein a plurality of the exhaust regions are provided along a circumference of the mounting table. 如申請專利範圍第7項之基板處理裝置,其中, 來自各個該排氣區域的排氣量係相同。The substrate processing apparatus of claim 7, wherein the amount of exhaust gas from each of the exhaust regions is the same.
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